From 81f450124364e5bdd164bacae144b13fd717a589 Mon Sep 17 00:00:00 2001 From: pkuLmq <1900011062@pku.edu.cn> Date: Tue, 20 Aug 2024 23:56:56 +0800 Subject: [PATCH] debug for test 7 --- test/corrtest.cpp | 8 +- test/logs | 90428 ++++++++++++++++++++++++++++++++++++++++++ test/testLoopReport | 4 + 3 files changed, 90436 insertions(+), 4 deletions(-) create mode 100644 test/logs create mode 100644 test/testLoopReport diff --git a/test/corrtest.cpp b/test/corrtest.cpp index 1b65f35f..edc65d0e 100644 --- a/test/corrtest.cpp +++ b/test/corrtest.cpp @@ -71,10 +71,10 @@ float aachenBomb4 = readBomb(192,"aachenBomb2D/data_T.xy"); // } TEST(corrtest,dfLowMachFoam_2DaachenBomb){ - EXPECT_NEAR(aachenBomb1,809.095,0.0001); - EXPECT_NEAR(aachenBomb2,1770.21,0.0001); - EXPECT_NEAR(aachenBomb3,917.437,0.0001); - EXPECT_NEAR(aachenBomb4,2474.36,0.0001); + EXPECT_NEAR(aachenBomb1,808.909,0.0001); + EXPECT_NEAR(aachenBomb2,1749.93,0.0001); + EXPECT_NEAR(aachenBomb3,903.652,0.0001); + EXPECT_NEAR(aachenBomb4,2478.74,0.0001); } float readmaxTH2(){ diff --git a/test/logs b/test/logs new file mode 100644 index 00000000..d3548a80 --- /dev/null +++ b/test/logs @@ -0,0 +1,90428 @@ +/*---------------------------------------------------------------------------*\ + ========= | + \\ / F ield | OpenFOAM: The Open Source CFD Toolbox + \\ / O peration | Website: https://openfoam.org + \\ / A nd | Version: 7 + \\/ M anipulation | +\*---------------------------------------------------------------------------*/ +Build : 7-1ff648926f77 +Exec : postProcess -func sample +Date : Aug 20 2024 +Time : 23:48:19 +Host : "lmqLab" +PID : 29864 +I/O : uncollated +Case : /home/lmq/deepflame-dev/test/aachenBomb_2D +nProcs : 1 +sigFpe : Enabling floating point exception trapping (FOAM_SIGFPE). +fileModificationChecking : Monitoring run-time modified files using timeStampMaster (fileModificationSkew 10) +allowSystemOperations : Allowing user-supplied system call operations + +// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // +Create time + +Duplicate entry NSRDSfunc0 in runtime selection table thermophysicalFunction +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam22thermophysicalFunction31adddictionaryConstructorToTableINS_10NSRDSfunc0EEC1ERKNS_4wordE+0x13a) [0x7f561445f6fa] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3c9ac) [0x7f560f2889ac] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry NSRDSfunc1 in runtime selection table thermophysicalFunction +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam22thermophysicalFunction31adddictionaryConstructorToTableINS_10NSRDSfunc1EEC1ERKNS_4wordE+0x13a) [0x7f561445fe5a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3ccbc) [0x7f560f288cbc] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry NSRDSfunc2 in runtime selection table thermophysicalFunction +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam22thermophysicalFunction31adddictionaryConstructorToTableINS_10NSRDSfunc2EEC2ERKNS_4wordE+0x13a) [0x7f561446052a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3cfcc) [0x7f560f288fcc] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry NSRDSfunc3 in runtime selection table thermophysicalFunction +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam22thermophysicalFunction31adddictionaryConstructorToTableINS_10NSRDSfunc3EEC1ERKNS_4wordE+0x13a) [0x7f5614460bea] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3d2dc) [0x7f560f2892dc] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry NSRDSfunc4 in runtime selection table thermophysicalFunction +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam22thermophysicalFunction31adddictionaryConstructorToTableINS_10NSRDSfunc4EEC1ERKNS_4wordE+0x13a) [0x7f561446139a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3d5ec) [0x7f560f2895ec] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry NSRDSfunc5 in runtime selection table thermophysicalFunction +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam22thermophysicalFunction31adddictionaryConstructorToTableINS_10NSRDSfunc5EEC2ERKNS_4wordE+0x13a) [0x7f5614461a5a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3d8fc) [0x7f560f2898fc] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry NSRDSfunc6 in runtime selection table thermophysicalFunction +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam22thermophysicalFunction31adddictionaryConstructorToTableINS_10NSRDSfunc6EEC2ERKNS_4wordE+0x13a) [0x7f561446245a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3dc0c) [0x7f560f289c0c] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry NSRDSfunc7 in runtime selection table thermophysicalFunction +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam22thermophysicalFunction31adddictionaryConstructorToTableINS_10NSRDSfunc7EEC2ERKNS_4wordE+0x13a) [0x7f5614462bda] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3df1c) [0x7f560f289f1c] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry NSRDSfunc14 in runtime selection table thermophysicalFunction +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam22thermophysicalFunction31adddictionaryConstructorToTableINS_11NSRDSfunc14EEC1ERKNS_4wordE+0x13a) [0x7f56144635ca] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3e230) [0x7f560f28a230] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry APIdiffCoefFunc in runtime selection table thermophysicalFunction +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam22thermophysicalFunction31adddictionaryConstructorToTableINS_15APIdiffCoefFuncEEC2ERKNS_4wordE+0x13a) [0x7f561446426a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3e547) [0x7f560f28a547] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry H2O in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_3H2OEEC2ERKNS_4wordE+0x13a) [0x7f5614475a0a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3ec9b) [0x7f560f28ac9b] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry H2O in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_3H2OEEC1ERKNS_4wordE+0x13a) [0x7f56144761ba] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3ecc3) [0x7f560f28acc3] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C7H16 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_5C7H16EEC1ERKNS_4wordE+0x13a) [0x7f561447ac8a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3edab) [0x7f560f28adab] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C7H16 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_5C7H16EEC1ERKNS_4wordE+0x13a) [0x7f561447af8a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3edd3) [0x7f560f28add3] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C12H26 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_6C12H26EEC2ERKNS_4wordE+0x13a) [0x7f561447f76a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3eebb) [0x7f560f28aebb] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C12H26 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_6C12H26EEC1ERKNS_4wordE+0x13a) [0x7f561447fa6a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3eee3) [0x7f560f28aee3] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C10H22 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_6C10H22EEC2ERKNS_4wordE+0x13a) [0x7f561448424a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3efcb) [0x7f560f28afcb] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C10H22 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_6C10H22EEC1ERKNS_4wordE+0x13a) [0x7f561448454a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3eff3) [0x7f560f28aff3] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C8H18 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_5C8H18EEC2ERKNS_4wordE+0x13a) [0x7f5614488d2a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3f0db) [0x7f560f28b0db] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C8H18 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_5C8H18EEC1ERKNS_4wordE+0x13a) [0x7f561448902a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3f103) [0x7f560f28b103] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry IC8H18 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_6IC8H18EEC1ERKNS_4wordE+0x13a) [0x7f561448d81a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3f1eb) [0x7f560f28b1eb] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry IC8H18 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_6IC8H18EEC2ERKNS_4wordE+0x13a) [0x7f561448db1a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3f213) [0x7f560f28b213] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C4H10O in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_6C4H10OEEC2ERKNS_4wordE+0x13a) [0x7f56144922fa] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3f2fb) [0x7f560f28b2fb] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C4H10O in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_6C4H10OEEC1ERKNS_4wordE+0x13a) [0x7f56144925fa] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3f323) [0x7f560f28b323] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C2H6O in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_5C2H6OEEC1ERKNS_4wordE+0x13a) [0x7f5614496dea] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3f40b) [0x7f560f28b40b] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C2H6O in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_5C2H6OEEC1ERKNS_4wordE+0x13a) [0x7f56144970ea] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3f433) [0x7f560f28b433] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry IDEA in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_4IDEAEEC2ERKNS_4wordE+0x13a) [0x7f561449b8ca] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3f51b) [0x7f560f28b51b] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry IDEA in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_4IDEAEEC2ERKNS_4wordE+0x13a) [0x7f561449bbca] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3f543) [0x7f560f28b543] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry aC11H10 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_9aC10H7CH3EEC1ERKNS_4wordE+0x13a) [0x7f56144a03aa] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3f62b) [0x7f560f28b62b] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry aC11H10 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_9aC10H7CH3EEC1ERKNS_4wordE+0x13a) [0x7f56144a06aa] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3f653) [0x7f560f28b653] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry bC11H10 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_9bC10H7CH3EEC2ERKNS_4wordE+0x13a) [0x7f56144a4e8a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3f73b) [0x7f560f28b73b] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry bC11H10 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_9bC10H7CH3EEC2ERKNS_4wordE+0x13a) [0x7f56144a518a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3f763) [0x7f560f28b763] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C8H10 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_5C8H10EEC1ERKNS_4wordE+0x13a) [0x7f56144a996a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3f84b) [0x7f560f28b84b] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C8H10 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_5C8H10EEC1ERKNS_4wordE+0x13a) [0x7f56144a9c6a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3f873) [0x7f560f28b873] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C16H34 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_6C16H34EEC1ERKNS_4wordE+0x13a) [0x7f56144ae44a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3f95b) [0x7f560f28b95b] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C16H34 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_6C16H34EEC1ERKNS_4wordE+0x13a) [0x7f56144ae74a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3f983) [0x7f560f28b983] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C9H20 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_5C9H20EEC1ERKNS_4wordE+0x13a) [0x7f56144b2f2a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3fa6b) [0x7f560f28ba6b] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C9H20 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_5C9H20EEC1ERKNS_4wordE+0x13a) [0x7f56144b322a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3fa93) [0x7f560f28ba93] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C6H6 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_4C6H6EEC2ERKNS_4wordE+0x13a) [0x7f56144b7a0a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3fb7b) [0x7f560f28bb7b] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C6H6 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_4C6H6EEC2ERKNS_4wordE+0x13a) [0x7f56144b7d0a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3fba3) [0x7f560f28bba3] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C7H8 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_4C7H8EEC2ERKNS_4wordE+0x13a) [0x7f56144bc4ea] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3fc8b) [0x7f560f28bc8b] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C7H8 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_4C7H8EEC1ERKNS_4wordE+0x13a) [0x7f56144bc7ea] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3fcb3) [0x7f560f28bcb3] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C6H14 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_5C6H14EEC2ERKNS_4wordE+0x13a) [0x7f56144c0fca] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3fd9b) [0x7f560f28bd9b] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C6H14 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_5C6H14EEC1ERKNS_4wordE+0x13a) [0x7f56144c12ca] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3fdc3) [0x7f560f28bdc3] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C13H28 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_6C13H28EEC1ERKNS_4wordE+0x13a) [0x7f56144c5aaa] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3feab) [0x7f560f28beab] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C13H28 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_6C13H28EEC1ERKNS_4wordE+0x13a) [0x7f56144c5daa] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3fed3) [0x7f560f28bed3] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C14H30 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_6C14H30EEC1ERKNS_4wordE+0x13a) [0x7f56144ca58a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3ffbb) [0x7f560f28bfbb] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C14H30 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_6C14H30EEC1ERKNS_4wordE+0x13a) [0x7f56144ca88a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x3ffe3) [0x7f560f28bfe3] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C3H8 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_4C3H8EEC2ERKNS_4wordE+0x13a) [0x7f56144cf35a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x400cb) [0x7f560f28c0cb] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C3H8 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_4C3H8EEC1ERKNS_4wordE+0x13a) [0x7f56144cf65a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x400f3) [0x7f560f28c0f3] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C3H6O in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_5C3H6OEEC1ERKNS_4wordE+0x13a) [0x7f56144d3e3a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x401db) [0x7f560f28c1db] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C3H6O in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_5C3H6OEEC1ERKNS_4wordE+0x13a) [0x7f56144d413a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x40203) [0x7f560f28c203] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C2H6 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_4C2H6EEC2ERKNS_4wordE+0x13a) [0x7f56144d8bfa] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x402eb) [0x7f560f28c2eb] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C2H6 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_4C2H6EEC2ERKNS_4wordE+0x13a) [0x7f56144d8efa] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x40313) [0x7f560f28c313] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry CH3OH in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_5CH3OHEEC2ERKNS_4wordE+0x13a) [0x7f56144dd6da] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x403fb) [0x7f560f28c3fb] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry CH3OH in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_5CH3OHEEC2ERKNS_4wordE+0x13a) [0x7f56144dd9da] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x40423) [0x7f560f28c423] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C2H5OH in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_6C2H5OHEEC2ERKNS_4wordE+0x13a) [0x7f56144e206a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x4050b) [0x7f560f28c50b] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C2H5OH in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_6C2H5OHEEC1ERKNS_4wordE+0x13a) [0x7f56144e236a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x40533) [0x7f560f28c533] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry Ar in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_2ArEEC2ERKNS_4wordE+0x13a) [0x7f56144e6a4a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x4061b) [0x7f560f28c61b] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry Ar in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_2ArEEC2ERKNS_4wordE+0x13a) [0x7f56144e6d4a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x40643) [0x7f560f28c643] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry N2 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_2N2EEC1ERKNS_4wordE+0x13a) [0x7f56144eb53a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x4072b) [0x7f560f28c72b] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry N2 in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_2N2EEC1ERKNS_4wordE+0x13a) [0x7f56144eb83a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x40753) [0x7f560f28c753] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry MB in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_2MBEEC2ERKNS_4wordE+0x13a) [0x7f56144f000a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x4083b) [0x7f560f28c83b] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry MB in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_2MBEEC2ERKNS_4wordE+0x13a) [0x7f56144f030a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x40863) [0x7f560f28c863] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry CH4N2O in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_6CH4N2OEEC2ERKNS_4wordE+0x13a) [0x7f56144f4b7a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x4094b) [0x7f560f28c94b] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry CH4N2O in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_6CH4N2OEEC2ERKNS_4wordE+0x13a) [0x7f56144f4e7a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x40973) [0x7f560f28c973] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry nC3H8O in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_6nC3H8OEEC1ERKNS_4wordE+0x13a) [0x7f56144f970a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x40a5b) [0x7f560f28ca5b] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry nC3H8O in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_6nC3H8OEEC2ERKNS_4wordE+0x13a) [0x7f56144f9a0a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x40a83) [0x7f560f28ca83] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry iC3H8O in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties21addConstructorToTableINS_6iC3H8OEEC1ERKNS_4wordE+0x13a) [0x7f56144fe29a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x40b6b) [0x7f560f28cb6b] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry iC3H8O in runtime selection table liquidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam16liquidProperties31adddictionaryConstructorToTableINS_6iC3H8OEEC2ERKNS_4wordE+0x13a) [0x7f56144fe59a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x40b93) [0x7f560f28cb93] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry ash in runtime selection table solidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam15solidProperties21addConstructorToTableINS_3ashEEC1ERKNS_4wordE+0x13a) [0x7f5614504c4a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x41060) [0x7f560f28d060] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry ash in runtime selection table solidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam15solidProperties31adddictionaryConstructorToTableINS_3ashEEC1ERKNS_4wordE+0x13a) [0x7f56145053fa] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x41088) [0x7f560f28d088] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C in runtime selection table solidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam15solidProperties21addConstructorToTableINS_1CEEC1ERKNS_4wordE+0x13a) [0x7f561450599a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x41180) [0x7f560f28d180] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry C in runtime selection table solidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam15solidProperties31adddictionaryConstructorToTableINS_1CEEC2ERKNS_4wordE+0x13a) [0x7f5614505c9a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x411a8) [0x7f560f28d1a8] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry CaCO3 in runtime selection table solidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam15solidProperties21addConstructorToTableINS_5CaCO3EEC2ERKNS_4wordE+0x13a) [0x7f561450623a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x412a0) [0x7f560f28d2a0] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry CaCO3 in runtime selection table solidProperties +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libthermophysicalProperties.so(_ZN4Foam15solidProperties31adddictionaryConstructorToTableINS_5CaCO3EEC1ERKNS_4wordE+0x13a) [0x7f561450653a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfThermophysicalProperties.so(+0x412c8) [0x7f560f28d2c8] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry fixedEnergy in runtime selection table fvPatchField +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libfluidThermophysicalModels.so(_ZN4Foam12fvPatchFieldIdE26addpatchConstructorToTableINS_29fixedEnergyFvPatchScalarFieldEEC1ERKNS_4wordE+0x13a) [0x7f561a401a0a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfFluidThermophysicalModels.so(+0x2d780) [0x7f560f58a780] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry fixedEnergy in runtime selection table fvPatchField +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libfluidThermophysicalModels.so(_ZN4Foam12fvPatchFieldIdE32addpatchMapperConstructorToTableINS_29fixedEnergyFvPatchScalarFieldEEC1ERKNS_4wordE+0x13a) [0x7f561a40221a] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfFluidThermophysicalModels.so(+0x2d7a8) [0x7f560f58a7a8] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry fixedEnergy in runtime selection table fvPatchField +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libfluidThermophysicalModels.so(_ZN4Foam12fvPatchFieldIdE31adddictionaryConstructorToTableINS_29fixedEnergyFvPatchScalarFieldEEC1ERKNS_4wordE+0x13a) [0x7f561a4029ca] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfFluidThermophysicalModels.so(+0x2d7d0) [0x7f560f58a7d0] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry gradientEnergy in runtime selection table fvPatchField +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libfluidThermophysicalModels.so(_ZN4Foam12fvPatchFieldIdE26addpatchConstructorToTableINS_32gradientEnergyFvPatchScalarFieldEEC2ERKNS_4wordE+0xfb) [0x7f561a407cbb] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfFluidThermophysicalModels.so(+0x2daa3) [0x7f560f58aaa3] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry gradientEnergy in runtime selection table fvPatchField +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libfluidThermophysicalModels.so(_ZN4Foam12fvPatchFieldIdE32addpatchMapperConstructorToTableINS_32gradientEnergyFvPatchScalarFieldEEC1ERKNS_4wordE+0xfb) [0x7f561a40803b] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfFluidThermophysicalModels.so(+0x2dacb) [0x7f560f58aacb] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry gradientEnergy in runtime selection table fvPatchField +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libfluidThermophysicalModels.so(_ZN4Foam12fvPatchFieldIdE31adddictionaryConstructorToTableINS_32gradientEnergyFvPatchScalarFieldEEC1ERKNS_4wordE+0xfb) [0x7f561a4083bb] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfFluidThermophysicalModels.so(+0x2daf3) [0x7f560f58aaf3] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry mixedEnergy in runtime selection table fvPatchField +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libfluidThermophysicalModels.so(_ZN4Foam12fvPatchFieldIdE26addpatchConstructorToTableINS_29mixedEnergyFvPatchScalarFieldEEC1ERKNS_4wordE+0xfb) [0x7f561a40db4b] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfFluidThermophysicalModels.so(+0x2dd9b) [0x7f560f58ad9b] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry mixedEnergy in runtime selection table fvPatchField +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libfluidThermophysicalModels.so(_ZN4Foam12fvPatchFieldIdE32addpatchMapperConstructorToTableINS_29mixedEnergyFvPatchScalarFieldEEC1ERKNS_4wordE+0xfb) [0x7f561a40dc8b] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfFluidThermophysicalModels.so(+0x2ddc3) [0x7f560f58adc3] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry mixedEnergy in runtime selection table fvPatchField +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libfluidThermophysicalModels.so(_ZN4Foam12fvPatchFieldIdE31adddictionaryConstructorToTableINS_29mixedEnergyFvPatchScalarFieldEEC2ERKNS_4wordE+0xfb) [0x7f561a40ddcb] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfFluidThermophysicalModels.so(+0x2ddeb) [0x7f560f58adeb] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry energyJump in runtime selection table fvPatchField +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libfluidThermophysicalModels.so(_ZN4Foam12fvPatchFieldIdE26addpatchConstructorToTableINS_28energyJumpFvPatchScalarFieldEEC1ERKNS_4wordE+0xfb) [0x7f561a4167ab] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfFluidThermophysicalModels.so(+0x2deee) [0x7f560f58aeee] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry energyJump in runtime selection table fvPatchField +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libfluidThermophysicalModels.so(_ZN4Foam12fvPatchFieldIdE32addpatchMapperConstructorToTableINS_28energyJumpFvPatchScalarFieldEEC1ERKNS_4wordE+0xfb) [0x7f561a4168eb] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfFluidThermophysicalModels.so(+0x2df16) [0x7f560f58af16] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry energyJump in runtime selection table fvPatchField +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libfluidThermophysicalModels.so(_ZN4Foam12fvPatchFieldIdE31adddictionaryConstructorToTableINS_28energyJumpFvPatchScalarFieldEEC1ERKNS_4wordE+0xfb) [0x7f561a416a2b] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfFluidThermophysicalModels.so(+0x2df3e) [0x7f560f58af3e] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry energyJumpAMI in runtime selection table fvPatchField +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libfluidThermophysicalModels.so(_ZN4Foam12fvPatchFieldIdE26addpatchConstructorToTableINS_31energyJumpAMIFvPatchScalarFieldEEC2ERKNS_4wordE+0xfb) [0x7f561a41cabb] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfFluidThermophysicalModels.so(+0x2e04b) [0x7f560f58b04b] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry energyJumpAMI in runtime selection table fvPatchField +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libfluidThermophysicalModels.so(_ZN4Foam12fvPatchFieldIdE32addpatchMapperConstructorToTableINS_31energyJumpAMIFvPatchScalarFieldEEC2ERKNS_4wordE+0xfb) [0x7f561a41cbfb] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfFluidThermophysicalModels.so(+0x2e073) [0x7f560f58b073] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry energyJumpAMI in runtime selection table fvPatchField +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libfluidThermophysicalModels.so(_ZN4Foam12fvPatchFieldIdE31adddictionaryConstructorToTableINS_31energyJumpAMIFvPatchScalarFieldEEC1ERKNS_4wordE+0xfb) [0x7f561a41cd3b] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfFluidThermophysicalModels.so(+0x2e09b) [0x7f560f58b09b] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry laminar in runtime selection table TurbulenceModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam15TurbulenceModelINS_17geometricOneFieldENS_14GeometricFieldIdNS_12fvPatchFieldENS_7volMeshEEENS_27compressibleTurbulenceModelENS_11fluidThermoEE31adddictionaryConstructorToTableINS_12laminarModelINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelIS7_EEEEEEEC2ERKNS_4wordE+0xac) [0x7f561ac54e7c] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xa9710) [0x7f560c802710] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry RAS in runtime selection table TurbulenceModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam15TurbulenceModelINS_17geometricOneFieldENS_14GeometricFieldIdNS_12fvPatchFieldENS_7volMeshEEENS_27compressibleTurbulenceModelENS_11fluidThermoEE31adddictionaryConstructorToTableINS_8RASModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelIS7_EEEEEEEEEC2ERKNS_4wordE+0xac) [0x7f561ac54f4c] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xa97b6) [0x7f560c8027b6] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry LES in runtime selection table TurbulenceModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam15TurbulenceModelINS_17geometricOneFieldENS_14GeometricFieldIdNS_12fvPatchFieldENS_7volMeshEEENS_27compressibleTurbulenceModelENS_11fluidThermoEE31adddictionaryConstructorToTableINS_8LESModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelIS7_EEEEEEEEEC1ERKNS_4wordE+0xac) [0x7f561ac5501c] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xa985c) [0x7f560c80285c] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry Stokes in runtime selection table laminarModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam12laminarModelINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEE31adddictionaryConstructorToTableINS_13laminarModels6StokesIS5_EEEC1ERKNS_4wordE+0xac) [0x7f561ac5560c] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xa9902) [0x7f560c802902] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry generalizedNewtonian in runtime selection table laminarModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam12laminarModelINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEE31adddictionaryConstructorToTableINS_13laminarModels20generalizedNewtonianIS5_EEEC2ERKNS_4wordE+0xac) [0x7f561ac556dc] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xa99a8) [0x7f560c8029a8] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry Maxwell in runtime selection table laminarModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam12laminarModelINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEE31adddictionaryConstructorToTableINS_13laminarModels7MaxwellIS5_EEEC1ERKNS_4wordE+0xac) [0x7f561ac557ac] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xa9a4e) [0x7f560c802a4e] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry Giesekus in runtime selection table laminarModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam12laminarModelINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEE31adddictionaryConstructorToTableINS_13laminarModels8GiesekusIS5_EEEC2ERKNS_4wordE+0xac) [0x7f561ac5587c] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xa9af4) [0x7f560c802af4] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry SpalartAllmaras in runtime selection table RASModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8RASModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9RASModels15SpalartAllmarasIS7_EEEC2ERKNS_4wordE+0xac) [0x7f561ac5816c] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xa9b9a) [0x7f560c802b9a] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry kEpsilon in runtime selection table RASModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8RASModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9RASModels8kEpsilonIS7_EEEC2ERKNS_4wordE+0xac) [0x7f561ac5823c] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xa9c40) [0x7f560c802c40] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry RNGkEpsilon in runtime selection table RASModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8RASModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9RASModels11RNGkEpsilonIS7_EEEC2ERKNS_4wordE+0xac) [0x7f561ac5830c] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xa9ce6) [0x7f560c802ce6] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry realizableKE in runtime selection table RASModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8RASModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9RASModels12realizableKEIS7_EEEC2ERKNS_4wordE+0xac) [0x7f561ac583dc] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xa9d8c) [0x7f560c802d8c] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry buoyantKEpsilon in runtime selection table RASModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8RASModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9RASModels15buoyantKEpsilonIS7_EEEC1ERKNS_4wordE+0xac) [0x7f561ac584ac] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xa9e32) [0x7f560c802e32] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry LaunderSharmaKE in runtime selection table RASModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8RASModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9RASModels15LaunderSharmaKEIS7_EEEC2ERKNS_4wordE+0xac) [0x7f561ac5857c] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xa9ed8) [0x7f560c802ed8] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry kOmega in runtime selection table RASModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8RASModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9RASModels6kOmegaIS7_EEEC2ERKNS_4wordE+0xac) [0x7f561ac5864c] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xa9f7e) [0x7f560c802f7e] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry kOmegaSST in runtime selection table RASModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8RASModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9RASModels9kOmegaSSTIS7_EEEC1ERKNS_4wordE+0xac) [0x7f561ac5871c] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xaa024) [0x7f560c803024] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry kOmegaSSTSAS in runtime selection table RASModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8RASModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9RASModels12kOmegaSSTSASIS7_EEEC1ERKNS_4wordE+0xac) [0x7f561ac587ec] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xaa0ca) [0x7f560c8030ca] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry kOmegaSSTLM in runtime selection table RASModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8RASModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9RASModels11kOmegaSSTLMIS7_EEEC1ERKNS_4wordE+0xac) [0x7f561ac588bc] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xaa170) [0x7f560c803170] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry v2f in runtime selection table RASModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8RASModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9RASModels3v2fIS7_EEEC1ERKNS_4wordE+0xac) [0x7f561ac5898c] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xaa216) [0x7f560c803216] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry LRR in runtime selection table RASModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8RASModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9RASModels3LRRIS7_EEEC1ERKNS_4wordE+0xac) [0x7f561ac58a5c] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xaa2bc) [0x7f560c8032bc] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry SSG in runtime selection table RASModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8RASModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9RASModels3SSGIS7_EEEC1ERKNS_4wordE+0xac) [0x7f561ac58b2c] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xaa362) [0x7f560c803362] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry Smagorinsky in runtime selection table LESModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8LESModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9LESModels11SmagorinskyIS7_EEEC1ERKNS_4wordE+0xac) [0x7f561ac591cc] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xaa408) [0x7f560c803408] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry WALE in runtime selection table LESModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8LESModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9LESModels4WALEIS7_EEEC1ERKNS_4wordE+0xac) [0x7f561ac5929c] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xaa4ae) [0x7f560c8034ae] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry kEqn in runtime selection table LESModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8LESModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9LESModels4kEqnIS7_EEEC1ERKNS_4wordE+0xac) [0x7f561ac5936c] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xaa554) [0x7f560c803554] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry dynamicKEqn in runtime selection table LESModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8LESModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9LESModels11dynamicKEqnIS7_EEEC1ERKNS_4wordE+0xac) [0x7f561ac5943c] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xaa5fa) [0x7f560c8035fa] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry dynamicLagrangian in runtime selection table LESModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8LESModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9LESModels17dynamicLagrangianIS7_EEEC2ERKNS_4wordE+0xac) [0x7f561ac5950c] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xaa6a0) [0x7f560c8036a0] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry kOmegaSSTDES in runtime selection table LESModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8LESModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9LESModels12kOmegaSSTDESIS7_EEEC2ERKNS_4wordE+0xac) [0x7f561ac595dc] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xaa746) [0x7f560c803746] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry SpalartAllmarasDES in runtime selection table LESModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8LESModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9LESModels18SpalartAllmarasDESIS7_EEEC1ERKNS_4wordE+0xac) [0x7f561ac596ac] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xaa7ec) [0x7f560c8037ec] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry SpalartAllmarasDDES in runtime selection table LESModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8LESModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9LESModels19SpalartAllmarasDDESIS7_EEEC2ERKNS_4wordE+0xac) [0x7f561ac5977c] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xaa892) [0x7f560c803892] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry SpalartAllmarasIDDES in runtime selection table LESModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8LESModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9LESModels20SpalartAllmarasIDDESIS7_EEEC1ERKNS_4wordE+0xac) [0x7f561ac5984c] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xaa938) [0x7f560c803938] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry DeardorffDiffStress in runtime selection table LESModel +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam8LESModelINS_15EddyDiffusivityINS_18ThermalDiffusivityINS_27CompressibleTurbulenceModelINS_11fluidThermoEEEEEEEE31adddictionaryConstructorToTableINS_9LESModels19DeardorffDiffStressIS7_EEEC1ERKNS_4wordE+0xac) [0x7f561ac5991c] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xaa9de) [0x7f560c8039de] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry compressible::alphatWallFunction in runtime selection table fvPatchField +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam12fvPatchFieldIdE26addpatchConstructorToTableINS_12compressible36alphatWallFunctionFvPatchScalarFieldEEC1ERKNS_4wordE+0xfb) [0x7f561ad80bab] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xaab2f) [0x7f560c803b2f] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry compressible::alphatWallFunction in runtime selection table fvPatchField +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam12fvPatchFieldIdE32addpatchMapperConstructorToTableINS_12compressible36alphatWallFunctionFvPatchScalarFieldEEC2ERKNS_4wordE+0xfb) [0x7f561ad80ceb] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xaab57) [0x7f560c803b57] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Duplicate entry compressible::alphatWallFunction in runtime selection table fvPatchField +#0 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam5error14safePrintStackERSo+0x3e) [0x7f56163f51ae] +#1 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libcompressibleTurbulenceModels.so(_ZN4Foam12fvPatchFieldIdE31adddictionaryConstructorToTableINS_12compressible36alphatWallFunctionFvPatchScalarFieldEEC1ERKNS_4wordE+0xfb) [0x7f561ad80e2b] +#2 /home/lmq/deepflame-dev/platforms/linux64GccDPInt32Opt/lib/libdfCompressibleTurbulenceModels.so(+0xaab7f) [0x7f560c803b7f] +#3 /lib64/ld-linux-x86-64.so.2(+0x108d3) [0x7f561b9118d3] +#4 /lib64/ld-linux-x86-64.so.2(+0x1539f) [0x7f561b91639f] +#5 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#6 /lib64/ld-linux-x86-64.so.2(+0x1496a) [0x7f561b91596a] +#7 /lib/x86_64-linux-gnu/libdl.so.2(+0xf96) [0x7f5615a0ef96] +#8 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_exception+0x6f) [0x7f56151d216f] +#9 /lib/x86_64-linux-gnu/libc.so.6(_dl_catch_error+0x2f) [0x7f56151d21ff] +#10 /lib/x86_64-linux-gnu/libdl.so.2(+0x1745) [0x7f5615a0f745] +#11 /lib/x86_64-linux-gnu/libdl.so.2(dlopen+0x71) [0x7f5615a0f051] +#12 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam6dlOpenERKNS_8fileNameEb+0x2e) [0x7f56163eecce] +#13 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_8fileNameEb+0x13e) [0x7f561607f61e] +#14 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam14dlLibraryTable4openERKNS_10dictionaryERKNS_4wordE+0x1d5) [0x7f561607fc95] +#15 /opt/openfoam7/platforms/linux64GccDPInt32Opt/lib/libOpenFOAM.so(_ZN4Foam4TimeC1ERKNS_4wordERKNS_7argListES3_S3_+0x56d) [0x7f56160a9e4d] +#16 postProcess(+0x3a2c7) [0x55570e83a2c7] +#17 /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7) [0x7f561508cc87] +#18 postProcess(+0x3aeea) [0x55570e83aeea] +Create mesh for time = 0 + +Reading set description: + data + +Time = 0 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.0001 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.0002 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.0003 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.0004 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.0005 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.0006 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.0007 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.0008 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.0009 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.001 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.0011 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.0012 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.0013 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.0014 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.0015 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.0016 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.0017 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.0018 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.0019 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.002 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.0021 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.0022 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +Time = 0.0023 + +Reading fields: + volScalarFields: T + + +Executing functionObjects + +End + +/*---------------------------------------------------------------------------*\ + ========= | + \\ / F ield | OpenFOAM: The Open Source CFD Toolbox + \\ / O peration | Website: https://openfoam.org + \\ / A nd | Version: 7 + \\/ M anipulation | +\*---------------------------------------------------------------------------*/ +Build : 7-1ff648926f77 +Exec : blockMesh +Date : Aug 20 2024 +Time : 23:43:02 +Host : "lmqLab" +PID : 29406 +I/O : uncollated +Case : /home/lmq/deepflame-dev/test/aachenBomb_2D +nProcs : 1 +sigFpe : Enabling floating point exception trapping (FOAM_SIGFPE). +fileModificationChecking : Monitoring run-time modified files using timeStampMaster (fileModificationSkew 10) +allowSystemOperations : Allowing user-supplied system call operations + +// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // +Create time + +Creating block mesh from + "/home/lmq/deepflame-dev/test/aachenBomb_2D/system/blockMeshDict" +Creating block edges +No non-planar block faces defined +Creating topology blocks +Creating topology patches + +Creating block mesh topology + +Check topology + + Basic statistics + Number of internal faces : 0 + Number of boundary faces : 6 + Number of defined boundary faces : 6 + Number of undefined boundary faces : 0 + Checking patch -> block consistency + +Creating block offsets +Creating merge list . + +Creating polyMesh from blockMesh +Creating patches +Creating cells +Creating points with scale 0.001 + Block 0 cell size : + i : 2e-06 + j : 0.000487805 + k : 0.001 + +Writing polyMesh +---------------- +Mesh Information +---------------- + boundingBox: (-0.01 0 -1e-06) (0.01 0.1 1e-06) + nPoints: 8484 + nCells: 4100 + nFaces: 16541 + nInternalFaces: 8059 +---------------- +Patches +---------------- + patch 0 (start: 8059 size: 282) name: walls + patch 1 (start: 8341 size: 8200) name: empty + +End + +I/O : uncollated +Case : /home/lmq/deepflame-dev/test/aachenBomb_2D +nProcs : 1 +Create time + +Create mesh for time = 0 + + +PIMPLE: No convergence criteria found + + +PIMPLE: Operating solver in transient mode with 1 outer corrector +PIMPLE: Operating solver in PISO mode + + + +Reading g +Reading thermophysical properties + +Creating component thermo properties: + multi-component carrier - 5 species + liquids - 1 components + solids - 0 components +Reading field U + +Reading/calculating face flux field phi + +Creating turbulence model + +Selecting turbulence model type RAS +Selecting RAS turbulence model kEpsilon +RAS +{ + RASModel kEpsilon; + turbulence on; + printCoeffs on; + Cmu 0.09; + C1 1.44; + C2 1.92; + C3 0; + sigmak 1; + sigmaEps 1.3; +} + +Creating field dpdt + +Creating reaction model + +Selecting combustion model laminar +--- I am here in Cantera-construct --- +relTol_ === 1e-06 +absTol_ === 1e-10 + using integrated reaction rate +end Creating reaction model + +Combustion Model Name is confirmed as laminar +At initial time, min/max(T) = 800, 800 +Creating field kinetic energy K + +No MRF models present + + +Constructing reacting cloud +Constructing particle forces + Selecting particle force sphereDrag +Constructing cloud functions + none +Constructing particle injection models +Creating injector: model1 +Selecting injection model coneInjection + Constructing 2-D injection +Selecting distribution model RosinRammler +Selecting dispersion model none +Selecting patch interaction model standardWallInteraction +Selecting stochastic collision model none +Selecting surface film model none +Selecting U integration scheme Euler +Selecting heat transfer model RanzMarshall +Selecting T integration scheme analytical +Selecting composition model singlePhaseMixture +Selecting phase change model liquidEvaporationBoil +Participating liquid species: + C7H16 +Selecting AtomizationModel none +Selecting BreakupModel ReitzDiwakar +Average parcel mass: 3.2e-12 +Courant Number mean: 0 max: 0 + +Starting time loop + +Courant Number mean: 0 max: 0 +Time = 2.5e-06 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 1 new parcels + +Cloud: sprayCloud + Current number of parcels = 1 + Current mass in system = 1.41054e-13 + Linear momentum = (-4.54136e-15 -9.89944e-14 0) + |Linear momentum| = 9.90985e-14 + Linear kinetic energy = 3.48111e-14 + model1: + number of parcels added = 1 + mass introduced = 1.41062e-13 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.364, 380.364 + Mass transfer phase change = 7.43024e-18 + D10, D32, Dmax (mu) = 49.5377, 49.5377, 49.5377 + Liquid penetration 95% mass (m) = 1.76198e-06 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 1, Final residual = 2.02661e-08, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 1, Final residual = 2.02661e-08, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 1, Final residual = 1.31516e-09, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.998699, Final residual = 1.32096e-09, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 +DILUPBiCGStab: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 +DILUPBiCGStab: Solving for energy, Initial residual = 0.99998, Final residual = 1.32348e-09, No Iterations 1 +min/max(T) = 799.994, 800 +GAMG: Solving for p, Initial residual = 1, Final residual = 0.0544985, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.9055e-10, global = 8.40442e-11, cumulative = 8.40442e-11 +GAMG: Solving for p, Initial residual = 0.0138938, Final residual = 3.73171e-07, No Iterations 6 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.5644e-11, global = 8.56409e-11, cumulative = 1.69685e-10 +smoothSolver: Solving for epsilon, Initial residual = 0.00196078, Final residual = 1.04693e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 1, Final residual = 1.98968e-08, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.089001 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001464 s +Y Equations = 0.00243058 s +E Equations = 0.000652 s +p Equations = 0.003558 s +calculate parcels = 0.018261 s +chemistry correctThermo = 0.002521 s +turbulence correct = 0.001357 s +combustion correct(in Y) = 0.0766594 s +percentage of chemistry = 86.1332 % +percentage of rho/U/Y/E = 5.30734 % +========Time details of each equation======= +rhoEqn Time = 0.000326 s +rhoEqn assamble = 0.000245 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001464 s +UEqn assamble = 0.000993 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000471 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001893 s +YEqn assamble = 0.000653 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000319 s +YEqn correct boundary = 0 s +EEqn Time = 0.000518 s +EEqn assamble = 0.000365 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000153 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 0.14 s ClockTime = 1 s +Courant Number mean: 6.17562e-09 max: 3.32297e-06 +Time = 5e-06 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 1 new parcels + +Cloud: sprayCloud + Current number of parcels = 2 + Current mass in system = 2.95984e-13 + Linear momentum = (5.20428e-15 -2.57008e-13 0) + |Linear momentum| = 2.57061e-13 + Linear kinetic energy = 1.15773e-13 + model1: + number of parcels added = 2 + mass introduced = 2.96001e-13 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.094, 380.726 + Mass transfer phase change = 1.6854e-17 + D10, D32, Dmax (mu) = 53.764, 74.7661, 139.452 + Liquid penetration 95% mass (m) = 3.51681e-06 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.333613, Final residual = 2.96292e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.20833, Final residual = 3.71633e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.13013, Final residual = 1.32138e-10, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.839866, Final residual = 6.28412e-10, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 1, Final residual = 7.57322e-10, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 1, Final residual = 7.61091e-10, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.279105, Final residual = 1.80729e-10, No Iterations 1 +min/max(T) = 800, 800.003 +GAMG: Solving for p, Initial residual = 0.687749, Final residual = 0.0275047, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.33546e-10, global = 1.11292e-10, cumulative = 2.80977e-10 +GAMG: Solving for p, Initial residual = 0.0189788, Final residual = 5.14205e-07, No Iterations 6 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.08626e-10, global = 1.08618e-10, cumulative = 3.89595e-10 +smoothSolver: Solving for epsilon, Initial residual = 0.000956693, Final residual = 4.86101e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.52038, Final residual = 6.703e-09, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.081081 s +other Time = 1e-06 s +rho Equations = 7.5e-05 s +U Equations = 0.000932 s +Y Equations = 0.00245234 s +E Equations = 0.000618 s +p Equations = 0.00343 s +calculate parcels = 0.019796 s +chemistry correctThermo = 0.002818 s +turbulence correct = 0.001249 s +combustion correct(in Y) = 0.0693657 s +percentage of chemistry = 85.5511 % +percentage of rho/U/Y/E = 5.02872 % +========Time details of each equation======= +rhoEqn Time = 0.000267 s +rhoEqn assamble = 0.000206 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000932 s +UEqn assamble = 0.000482 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00045 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001861 s +YEqn assamble = 0.000603 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000357 s +YEqn correct boundary = 0 s +EEqn Time = 0.000473 s +EEqn assamble = 0.000321 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000152 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 0.22 s ClockTime = 1 s +Courant Number mean: 6.52715e-09 max: 4.11835e-06 +Time = 7.5e-06 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 2 new parcels + +Cloud: sprayCloud + Current number of parcels = 4 + Current mass in system = 6.15215e-13 + Linear momentum = (-8.95961e-15 -6.99386e-13 0) + |Linear momentum| = 6.99444e-13 + Linear kinetic energy = 4.29891e-13 + model1: + number of parcels added = 4 + mass introduced = 6.15257e-13 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.172, 381.087 + Mass transfer phase change = 4.15549e-17 + D10, D32, Dmax (mu) = 58.7046, 75.2578, 139.457 + Liquid penetration 95% mass (m) = 6.16289e-06 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.48027, Final residual = 4.52027e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.435201, Final residual = 7.26142e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.289895, Final residual = 1.54488e-10, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.20823, Final residual = 1.13648e-10, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.200365, Final residual = 1.09318e-10, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.200366, Final residual = 1.09908e-10, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.284497, Final residual = 1.64877e-10, No Iterations 1 +min/max(T) = 800, 800.005 +GAMG: Solving for p, Initial residual = 0.683268, Final residual = 0.0139429, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.94383e-10, global = 2.84489e-10, cumulative = 6.74084e-10 +GAMG: Solving for p, Initial residual = 0.0129966, Final residual = 3.47139e-07, No Iterations 6 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.84708e-10, global = 2.84702e-10, cumulative = 9.58786e-10 +smoothSolver: Solving for epsilon, Initial residual = 0.000911264, Final residual = 4.48378e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.268861, Final residual = 3.43629e-09, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.082328 s +other Time = 0 s +rho Equations = 9.7e-05 s +U Equations = 0.001078 s +Y Equations = 0.00249731 s +E Equations = 0.000623 s +p Equations = 0.00305 s +calculate parcels = 0.02192 s +chemistry correctThermo = 0.002755 s +turbulence correct = 0.001053 s +combustion correct(in Y) = 0.0710277 s +percentage of chemistry = 86.274 % +percentage of rho/U/Y/E = 5.21731 % +========Time details of each equation======= +rhoEqn Time = 0.000306 s +rhoEqn assamble = 0.000217 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001076 s +UEqn assamble = 0.000557 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000519 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001756 s +YEqn assamble = 0.000594 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000284 s +YEqn correct boundary = 0 s +EEqn Time = 0.000473 s +EEqn assamble = 0.000324 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000149 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 0.31 s ClockTime = 1 s +Courant Number mean: 1.00309e-08 max: 1.64196e-06 +Time = 1e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 7 new parcels + +Cloud: sprayCloud + Current number of parcels = 11 + Current mass in system = 1.75481e-12 + Linear momentum = (-7.48705e-14 -3.10192e-12 0) + |Linear momentum| = 3.10282e-12 + Linear kinetic energy = 3.01091e-12 + model1: + number of parcels added = 11 + mass introduced = 1.75493e-12 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.104, 381.448 + Mass transfer phase change = 1.1441e-16 + D10, D32, Dmax (mu) = 52.7735, 78.3171, 148.17 + Liquid penetration 95% mass (m) = 9.36682e-06 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.245329, Final residual = 3.52123e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.183518, Final residual = 3.607e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.331124, Final residual = 1.75536e-10, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.25958, Final residual = 1.43733e-10, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.25229, Final residual = 1.40611e-10, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.25229, Final residual = 1.41363e-10, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.322964, Final residual = 1.77822e-10, No Iterations 1 +min/max(T) = 799.998, 800.002 +GAMG: Solving for p, Initial residual = 0.374138, Final residual = 0.0116606, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.06574e-09, global = 8.38669e-10, cumulative = 1.79746e-09 +GAMG: Solving for p, Initial residual = 0.00961611, Final residual = 2.79189e-07, No Iterations 6 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.39732e-10, global = 8.39726e-10, cumulative = 2.63718e-09 +smoothSolver: Solving for epsilon, Initial residual = 0.000872571, Final residual = 4.18267e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.1807, Final residual = 2.29607e-09, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.078456 s +other Time = 0 s +rho Equations = 7.9e-05 s +U Equations = 0.000936 s +Y Equations = 0.00233715 s +E Equations = 0.00062 s +p Equations = 0.002916 s +calculate parcels = 0.024172 s +chemistry correctThermo = 0.002724 s +turbulence correct = 0.001041 s +combustion correct(in Y) = 0.0676718 s +percentage of chemistry = 86.2545 % +percentage of rho/U/Y/E = 5.06291 % +========Time details of each equation======= +rhoEqn Time = 0.000221 s +rhoEqn assamble = 0.000172 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 4.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000934 s +UEqn assamble = 0.000486 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000448 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001827 s +YEqn assamble = 0.000595 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000367 s +YEqn correct boundary = 0 s +EEqn Time = 0.000468 s +EEqn assamble = 0.000318 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00015 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 0.39 s ClockTime = 1 s +Courant Number mean: 1.17564e-08 max: 3.56175e-06 +Time = 1.25e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 2 new parcels + +Cloud: sprayCloud + Current number of parcels = 13 + Current mass in system = 2.09111e-12 + Linear momentum = (-3.29741e-14 -3.91127e-12 0) + |Linear momentum| = 3.91141e-12 + Linear kinetic energy = 4.00188e-12 + model1: + number of parcels added = 13 + mass introduced = 2.0913e-12 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.205, 381.921 + Mass transfer phase change = 1.94858e-16 + D10, D32, Dmax (mu) = 55.1767, 80.1639, 148.178 + Liquid penetration 95% mass (m) = 1.31229e-05 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.355742, Final residual = 3.69171e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.218379, Final residual = 3.98553e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0821069, Final residual = 4.15462e-11, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.22477, Final residual = 1.16634e-10, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.2363, Final residual = 1.22377e-10, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.2363, Final residual = 1.23045e-10, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.15766, Final residual = 8.55696e-11, No Iterations 1 +min/max(T) = 800, 800.056 +GAMG: Solving for p, Initial residual = 0.746958, Final residual = 0.0286604, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.98319e-09, global = 9.39238e-10, cumulative = 3.57642e-09 +GAMG: Solving for p, Initial residual = 0.012697, Final residual = 3.04483e-07, No Iterations 6 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.27268e-10, global = 9.27242e-10, cumulative = 4.50366e-09 +smoothSolver: Solving for epsilon, Initial residual = 0.000839052, Final residual = 3.93636e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.136287, Final residual = 1.72399e-09, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.092421 s +other Time = 1e-06 s +rho Equations = 8.1e-05 s +U Equations = 0.000934 s +Y Equations = 0.00246829 s +E Equations = 0.000656 s +p Equations = 0.002904 s +calculate parcels = 0.026635 s +chemistry correctThermo = 0.00269 s +turbulence correct = 0.001069 s +combustion correct(in Y) = 0.0814897 s +percentage of chemistry = 88.1723 % +percentage of rho/U/Y/E = 4.47873 % +========Time details of each equation======= +rhoEqn Time = 0.000222 s +rhoEqn assamble = 0.000172 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000933 s +UEqn assamble = 0.000484 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000449 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00185 s +YEqn assamble = 0.00064 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000352 s +YEqn correct boundary = 0 s +EEqn Time = 0.000502 s +EEqn assamble = 0.000348 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000154 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 0.48 s ClockTime = 1 s +Courant Number mean: 6.21321e-08 max: 2.97874e-05 +Time = 1.5e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 7 new parcels + +Cloud: sprayCloud + Current number of parcels = 20 + Current mass in system = 3.2735e-12 + Linear momentum = (-1.98351e-13 -7.62425e-12 0) + |Linear momentum| = 7.62683e-12 + Linear kinetic energy = 9.91288e-12 + model1: + number of parcels added = 20 + mass introduced = 3.27381e-12 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.141, 382.81 + Mass transfer phase change = 3.09989e-16 + D10, D32, Dmax (mu) = 60.6087, 87.9724, 148.186 + Liquid penetration 95% mass (m) = 1.76889e-05 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.304482, Final residual = 2.65668e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.191919, Final residual = 3.22386e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.12224, Final residual = 6.27184e-11, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.134564, Final residual = 6.98426e-11, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.135266, Final residual = 7.01855e-11, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.135266, Final residual = 7.05682e-11, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.139616, Final residual = 7.73874e-11, No Iterations 1 +min/max(T) = 800, 800.099 +GAMG: Solving for p, Initial residual = 0.438079, Final residual = 0.00631321, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.92588e-09, global = 1.3311e-09, cumulative = 5.83476e-09 +GAMG: Solving for p, Initial residual = 0.00434776, Final residual = 4.09347e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.32706e-09, global = 1.327e-09, cumulative = 7.16176e-09 +smoothSolver: Solving for epsilon, Initial residual = 0.000809578, Final residual = 3.74282e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.109525, Final residual = 1.38065e-09, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.084117 s +other Time = 0 s +rho Equations = 9.5e-05 s +U Equations = 0.000966 s +Y Equations = 0.00244376 s +E Equations = 0.000634 s +p Equations = 0.002174 s +calculate parcels = 0.029526 s +chemistry correctThermo = 0.002318 s +turbulence correct = 0.000979 s +combustion correct(in Y) = 0.0743742 s +percentage of chemistry = 88.4176 % +percentage of rho/U/Y/E = 4.92024 % +========Time details of each equation======= +rhoEqn Time = 0.00021 s +rhoEqn assamble = 0.000161 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 4.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000966 s +UEqn assamble = 0.000497 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000469 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001804 s +YEqn assamble = 0.000611 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000327 s +YEqn correct boundary = 0 s +EEqn Time = 0.000484 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000152 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 0.57 s ClockTime = 1 s +Courant Number mean: 1.16195e-07 max: 2.80839e-05 +Time = 1.75e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 10 new parcels + +Cloud: sprayCloud + Current number of parcels = 30 + Current mass in system = 4.99349e-12 + Linear momentum = (-3.48685e-13 -1.38751e-11 0) + |Linear momentum| = 1.38794e-11 + Linear kinetic energy = 2.13827e-11 + model1: + number of parcels added = 30 + mass introduced = 4.99407e-12 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.137, 383.694 + Mass transfer phase change = 5.78416e-16 + D10, D32, Dmax (mu) = 40.538, 76.8286, 148.193 + Liquid penetration 95% mass (m) = 2.27339e-05 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.19938, Final residual = 2.80166e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.135349, Final residual = 2.65833e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.244588, Final residual = 1.2092e-10, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.109309, Final residual = 5.51065e-11, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0995347, Final residual = 5.01658e-11, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0995347, Final residual = 5.04416e-11, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.190712, Final residual = 1.06499e-10, No Iterations 1 +min/max(T) = 800, 800.025 +GAMG: Solving for p, Initial residual = 0.380358, Final residual = 0.0131697, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.51462e-09, global = 3.07823e-09, cumulative = 1.024e-08 +GAMG: Solving for p, Initial residual = 0.011508, Final residual = 2.75996e-07, No Iterations 6 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.09394e-09, global = 3.09388e-09, cumulative = 1.33339e-08 +smoothSolver: Solving for epsilon, Initial residual = 0.000783327, Final residual = 3.57997e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0916315, Final residual = 1.15197e-09, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.082429 s +other Time = 1e-06 s +rho Equations = 6.9e-05 s +U Equations = 0.000816 s +Y Equations = 0.00240122 s +E Equations = 0.000786 s +p Equations = 0.002863 s +calculate parcels = 0.032305 s +chemistry correctThermo = 0.002731 s +turbulence correct = 0.001017 s +combustion correct(in Y) = 0.0716268 s +percentage of chemistry = 86.8951 % +percentage of rho/U/Y/E = 4.94028 % +========Time details of each equation======= +rhoEqn Time = 0.000213 s +rhoEqn assamble = 0.000168 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 4.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000813 s +UEqn assamble = 0.000419 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000394 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001896 s +YEqn assamble = 0.00062 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000415 s +YEqn correct boundary = 0 s +EEqn Time = 0.000635 s +EEqn assamble = 0.000457 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000178 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 0.65 s ClockTime = 1 s +Courant Number mean: 1.15587e-07 max: 3.68993e-05 +Time = 2e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 11 new parcels + +Cloud: sprayCloud + Current number of parcels = 41 + Current mass in system = 6.92719e-12 + Linear momentum = (-1.9017e-13 -2.18283e-11 0) + |Linear momentum| = 2.18291e-11 + Linear kinetic energy = 3.79277e-11 + model1: + number of parcels added = 41 + mass introduced = 6.92812e-12 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.165, 384.573 + Mass transfer phase change = 9.25147e-16 + D10, D32, Dmax (mu) = 43.9941, 81.384, 148.201 + Liquid penetration 95% mass (m) = 2.8367e-05 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.355583, Final residual = 3.07857e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.213172, Final residual = 3.74396e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.154849, Final residual = 7.44274e-11, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0960994, Final residual = 4.77863e-11, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0900478, Final residual = 4.49405e-11, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0900478, Final residual = 4.51884e-11, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.144323, Final residual = 7.76905e-11, No Iterations 1 +min/max(T) = 799.926, 800.002 +GAMG: Solving for p, Initial residual = 0.328903, Final residual = 0.00541368, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.12211e-09, global = 3.93526e-09, cumulative = 1.72691e-08 +GAMG: Solving for p, Initial residual = 0.00432647, Final residual = 3.31568e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.9965e-09, global = 3.99642e-09, cumulative = 2.12655e-08 +smoothSolver: Solving for epsilon, Initial residual = 0.000759758, Final residual = 3.44078e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0788219, Final residual = 9.88838e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.075777 s +other Time = 0 s +rho Equations = 7.3e-05 s +U Equations = 0.000918 s +Y Equations = 0.00223983 s +E Equations = 0.000516 s +p Equations = 0.002204 s +calculate parcels = 0.035948 s +chemistry correctThermo = 0.001966 s +turbulence correct = 0.000859 s +combustion correct(in Y) = 0.0668812 s +percentage of chemistry = 88.2605 % +percentage of rho/U/Y/E = 4.94454 % +========Time details of each equation======= +rhoEqn Time = 0.000188 s +rhoEqn assamble = 0.000148 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000918 s +UEqn assamble = 0.000469 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000449 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001672 s +YEqn assamble = 0.00055 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000283 s +YEqn correct boundary = 0 s +EEqn Time = 0.000397 s +EEqn assamble = 0.000271 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000126 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 0.73 s ClockTime = 1 s +Courant Number mean: 1.84484e-07 max: 6.41117e-05 +Time = 2.25e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 11 new parcels + +Cloud: sprayCloud + Current number of parcels = 52 + Current mass in system = 8.89926e-12 + Linear momentum = (-1.68424e-13 -3.11053e-11 0) + |Linear momentum| = 3.11057e-11 + Linear kinetic energy = 6.00967e-11 + model1: + number of parcels added = 52 + mass introduced = 8.9006e-12 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.172, 386.43 + Mass transfer phase change = 1.33677e-15 + D10, D32, Dmax (mu) = 47.0914, 84.4889, 148.208 + Liquid penetration 95% mass (m) = 3.43474e-05 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.305897, Final residual = 3.14381e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.289078, Final residual = 5.37147e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.112295, Final residual = 5.31359e-11, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0806642, Final residual = 3.95158e-11, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.076785, Final residual = 3.77768e-11, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0767851, Final residual = 3.79854e-11, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.10942, Final residual = 6.18621e-11, No Iterations 1 +min/max(T) = 799.81, 800.003 +GAMG: Solving for p, Initial residual = 0.339523, Final residual = 0.00499741, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.00876e-09, global = 4.7056e-09, cumulative = 2.59711e-08 +GAMG: Solving for p, Initial residual = 0.00290871, Final residual = 3.34195e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.7445e-09, global = 4.74438e-09, cumulative = 3.07155e-08 +smoothSolver: Solving for epsilon, Initial residual = 0.000738399, Final residual = 3.32029e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0691974, Final residual = 8.66648e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.083791 s +other Time = 1e-06 s +rho Equations = 9.2e-05 s +U Equations = 0.000963 s +Y Equations = 0.00244257 s +E Equations = 0.000701 s +p Equations = 0.002838 s +calculate parcels = 0.039765 s +chemistry correctThermo = 0.0027 s +turbulence correct = 0.001066 s +combustion correct(in Y) = 0.0728584 s +percentage of chemistry = 86.9526 % +percentage of rho/U/Y/E = 5.01076 % +========Time details of each equation======= +rhoEqn Time = 0.000252 s +rhoEqn assamble = 0.000187 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000962 s +UEqn assamble = 0.000506 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000456 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001844 s +YEqn assamble = 0.000613 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000364 s +YEqn correct boundary = 0 s +EEqn Time = 0.000532 s +EEqn assamble = 0.000372 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00016 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 0.82 s ClockTime = 1 s +Courant Number mean: 2.95432e-07 max: 7.88945e-05 +Time = 2.5e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 13 new parcels + +Cloud: sprayCloud + Current number of parcels = 65 + Current mass in system = 1.12674e-11 + Linear momentum = (-1.74815e-13 -4.34634e-11 0) + |Linear momentum| = 4.34638e-11 + Linear kinetic energy = 9.28993e-11 + model1: + number of parcels added = 65 + mass introduced = 1.12692e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.174, 388.511 + Mass transfer phase change = 1.82174e-15 + D10, D32, Dmax (mu) = 49.9526, 89.2573, 148.216 + Liquid penetration 95% mass (m) = 4.17685e-05 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.232122, Final residual = 3.12937e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.174991, Final residual = 3.53091e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0913283, Final residual = 4.22783e-11, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0681921, Final residual = 8.74385e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0649665, Final residual = 8.36833e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0649665, Final residual = 8.39451e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0897827, Final residual = 5.30379e-11, No Iterations 1 +min/max(T) = 799.659, 800.004 +GAMG: Solving for p, Initial residual = 0.211484, Final residual = 0.00230902, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.55688e-09, global = 5.52666e-09, cumulative = 3.62422e-08 +GAMG: Solving for p, Initial residual = 0.00132993, Final residual = 8.24527e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.59022e-09, global = 5.58974e-09, cumulative = 4.18319e-08 +smoothSolver: Solving for epsilon, Initial residual = 0.000718896, Final residual = 3.21483e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0617002, Final residual = 7.71736e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.08127 s +other Time = 0 s +rho Equations = 8.3e-05 s +U Equations = 0.000947 s +Y Equations = 0.00253557 s +E Equations = 0.000705 s +p Equations = 0.00271 s +calculate parcels = 0.044241 s +chemistry correctThermo = 0.002856 s +turbulence correct = 0.001114 s +combustion correct(in Y) = 0.0701894 s +percentage of chemistry = 86.3657 % +percentage of rho/U/Y/E = 5.25479 % +========Time details of each equation======= +rhoEqn Time = 0.000244 s +rhoEqn assamble = 0.000191 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000947 s +UEqn assamble = 0.00049 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000457 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00195 s +YEqn assamble = 0.000679 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000313 s +YEqn correct boundary = 0 s +EEqn Time = 0.000543 s +EEqn assamble = 0.000349 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000194 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 0.91 s ClockTime = 1 s +Courant Number mean: 4.57417e-07 max: 9.94665e-05 +Time = 2.75e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 10 new parcels + +Cloud: sprayCloud + Current number of parcels = 75 + Current mass in system = 1.31207e-11 + Linear momentum = (-1.76219e-13 -5.41497e-11 0) + |Linear momentum| = 5.415e-11 + Linear kinetic energy = 1.24092e-10 + model1: + number of parcels added = 75 + mass introduced = 1.31231e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.17, 390.565 + Mass transfer phase change = 2.39782e-15 + D10, D32, Dmax (mu) = 51.5543, 89.6185, 148.224 + Liquid penetration 95% mass (m) = 4.97559e-05 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.188952, Final residual = 2.95186e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.126027, Final residual = 2.7166e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.08027, Final residual = 9.8596e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0597068, Final residual = 7.63275e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0565984, Final residual = 7.29085e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0565984, Final residual = 7.31373e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0787027, Final residual = 4.73538e-11, No Iterations 1 +min/max(T) = 799.455, 800.007 +GAMG: Solving for p, Initial residual = 0.151219, Final residual = 0.0149432, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.62746e-08, global = 8.13541e-09, cumulative = 4.99673e-08 +GAMG: Solving for p, Initial residual = 0.0110312, Final residual = 5.17016e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.64029e-09, global = 6.63985e-09, cumulative = 5.66072e-08 +smoothSolver: Solving for epsilon, Initial residual = 0.000700972, Final residual = 3.12169e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0556942, Final residual = 6.95905e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.086839 s +other Time = 0 s +rho Equations = 0.000107 s +U Equations = 0.001081 s +Y Equations = 0.00208753 s +E Equations = 0.000538 s +p Equations = 0.002071 s +calculate parcels = 0.049305 s +chemistry correctThermo = 0.001964 s +turbulence correct = 0.000908 s +combustion correct(in Y) = 0.0779385 s +percentage of chemistry = 89.7505 % +percentage of rho/U/Y/E = 4.3915 % +========Time details of each equation======= +rhoEqn Time = 0.000225 s +rhoEqn assamble = 0.000177 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 4.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001079 s +UEqn assamble = 0.000595 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000484 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001443 s +YEqn assamble = 0.00053 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000114 s +YEqn correct boundary = 0 s +EEqn Time = 0.000419 s +EEqn assamble = 0.000276 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000143 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 1 s ClockTime = 1 s +Courant Number mean: 6.95388e-07 max: 0.000132056 +Time = 3e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 9 new parcels + +Cloud: sprayCloud + Current number of parcels = 84 + Current mass in system = 1.48034e-11 + Linear momentum = (-4.73202e-13 -6.46497e-11 0) + |Linear momentum| = 6.46514e-11 + Linear kinetic energy = 1.57318e-10 + model1: + number of parcels added = 84 + mass introduced = 1.48065e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.178, 392.591 + Mass transfer phase change = 3.05867e-15 + D10, D32, Dmax (mu) = 53.031, 90.4585, 148.231 + Liquid penetration 95% mass (m) = 5.83185e-05 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.158908, Final residual = 2.56211e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.102947, Final residual = 2.2646e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0700112, Final residual = 8.46057e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0526862, Final residual = 6.63273e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0498302, Final residual = 6.31827e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0498302, Final residual = 6.33827e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0696829, Final residual = 4.24643e-11, No Iterations 1 +min/max(T) = 799.203, 800.011 +GAMG: Solving for p, Initial residual = 0.114785, Final residual = 0.00813759, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.51496e-08, global = 9.18993e-09, cumulative = 6.57971e-08 +GAMG: Solving for p, Initial residual = 0.00621377, Final residual = 3.67116e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.61744e-09, global = 7.61701e-09, cumulative = 7.34141e-08 +smoothSolver: Solving for epsilon, Initial residual = 0.000684406, Final residual = 3.03874e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.050774, Final residual = 6.33934e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.069083 s +other Time = 0 s +rho Equations = 0.000175 s +U Equations = 0.001574 s +Y Equations = 0.00272674 s +E Equations = 0.000546 s +p Equations = 0.002641 s +calculate parcels = 0.057077 s +chemistry correctThermo = 0.001958 s +turbulence correct = 0.00108 s +combustion correct(in Y) = 0.0581903 s +percentage of chemistry = 84.2324 % +percentage of rho/U/Y/E = 7.26914 % +========Time details of each equation======= +rhoEqn Time = 0.000339 s +rhoEqn assamble = 0.000261 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001572 s +UEqn assamble = 0.000829 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000743 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001708 s +YEqn assamble = 0.000618 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -7e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000412 s +EEqn assamble = 0.000289 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000123 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 1.08 s ClockTime = 1 s +Courant Number mean: 9.8892e-07 max: 0.000163874 +Time = 3.25e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 18 new parcels + +Cloud: sprayCloud + Current number of parcels = 102 + Current mass in system = 1.81887e-11 + Linear momentum = (-8.334e-13 -8.74632e-11 0) + |Linear momentum| = 8.74672e-11 + Linear kinetic energy = 2.35406e-10 + model1: + number of parcels added = 102 + mass introduced = 1.81929e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.208, 394.589 + Mass transfer phase change = 4.17751e-15 + D10, D32, Dmax (mu) = 33.3575, 86.6006, 148.239 + Liquid penetration 95% mass (m) = 6.74793e-05 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.133456, Final residual = 2.1907e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0926703, Final residual = 1.95162e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0971679, Final residual = 4.23427e-11, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0527051, Final residual = 6.57831e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0445938, Final residual = 5.6509e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0445938, Final residual = 5.66885e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0866786, Final residual = 4.87427e-11, No Iterations 1 +min/max(T) = 798.602, 800.016 +GAMG: Solving for p, Initial residual = 0.165736, Final residual = 0.00417589, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.85786e-08, global = 1.27202e-08, cumulative = 8.61343e-08 +GAMG: Solving for p, Initial residual = 0.00293734, Final residual = 3.68453e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.28963e-08, global = 1.28956e-08, cumulative = 9.903e-08 +smoothSolver: Solving for epsilon, Initial residual = 0.000669014, Final residual = 2.96437e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0466683, Final residual = 5.82403e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.065088 s +other Time = 0 s +rho Equations = 0.000115 s +U Equations = 0.001086 s +Y Equations = 0.00226076 s +E Equations = 0.00052 s +p Equations = 0.002406 s +calculate parcels = 0.062128 s +chemistry correctThermo = 0.001997 s +turbulence correct = 0.000951 s +combustion correct(in Y) = 0.0555962 s +percentage of chemistry = 85.417 % +percentage of rho/U/Y/E = 6.1175 % +========Time details of each equation======= +rhoEqn Time = 0.000245 s +rhoEqn assamble = 0.000194 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001086 s +UEqn assamble = 0.00058 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000506 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001652 s +YEqn assamble = 0.000627 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00017 s +YEqn correct boundary = 0 s +EEqn Time = 0.000395 s +EEqn assamble = 0.000271 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000124 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 1.15 s ClockTime = 2 s +Courant Number mean: 1.6209e-06 max: 0.000362136 +Time = 3.5e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 10 new parcels + +Cloud: sprayCloud + Current number of parcels = 112 + Current mass in system = 2.01068e-11 + Linear momentum = (-1.24016e-12 -1.01352e-10 0) + |Linear momentum| = 1.01359e-10 + Linear kinetic energy = 2.86635e-10 + model1: + number of parcels added = 112 + mass introduced = 2.01121e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.2, 396.561 + Mass transfer phase change = 5.28974e-15 + D10, D32, Dmax (mu) = 34.637, 87.2495, 148.247 + Liquid penetration 95% mass (m) = 7.69351e-05 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.159871, Final residual = 1.97186e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.100452, Final residual = 2.06477e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0683425, Final residual = 8.04879e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0463341, Final residual = 5.77031e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0416231, Final residual = 5.27329e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0416231, Final residual = 5.29007e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0690299, Final residual = 4.24023e-11, No Iterations 1 +min/max(T) = 798.059, 800.019 +GAMG: Solving for p, Initial residual = 0.172542, Final residual = 0.0149907, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.28127e-08, global = 1.51072e-08, cumulative = 1.14137e-07 +GAMG: Solving for p, Initial residual = 0.0118711, Final residual = 9.77119e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.28221e-08, global = 1.28196e-08, cumulative = 1.26957e-07 +smoothSolver: Solving for epsilon, Initial residual = 0.000654669, Final residual = 2.89733e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0431907, Final residual = 5.38837e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.071619 s +other Time = 1e-06 s +rho Equations = 9.1e-05 s +U Equations = 0.000908 s +Y Equations = 0.00206593 s +E Equations = 0.000533 s +p Equations = 0.002112 s +calculate parcels = 0.067023 s +chemistry correctThermo = 0.001875 s +turbulence correct = 0.001022 s +combustion correct(in Y) = 0.0628171 s +percentage of chemistry = 87.7101 % +percentage of rho/U/Y/E = 5.02371 % +========Time details of each equation======= +rhoEqn Time = 0.000217 s +rhoEqn assamble = 0.00017 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 4.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000908 s +UEqn assamble = 0.000511 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000397 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001507 s +YEqn assamble = 0.000538 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000148 s +YEqn correct boundary = 0 s +EEqn Time = 0.00041 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000127 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 1.22 s ClockTime = 2 s +Courant Number mean: 2.23108e-06 max: 0.000367294 +Time = 3.75e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 15 new parcels + +Cloud: sprayCloud + Current number of parcels = 127 + Current mass in system = 2.29987e-11 + Linear momentum = (-7.04507e-13 -1.23757e-10 0) + |Linear momentum| = 1.23759e-10 + Linear kinetic energy = 3.7512e-10 + model1: + number of parcels added = 127 + mass introduced = 2.30053e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.209, 400.681 + Mass transfer phase change = 6.59606e-15 + D10, D32, Dmax (mu) = 36.3598, 88.327, 148.254 + Liquid penetration 95% mass (m) = 8.71103e-05 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.120888, Final residual = 1.83592e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0885155, Final residual = 1.86286e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0632787, Final residual = 7.34427e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.04304, Final residual = 5.32039e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0382638, Final residual = 4.82986e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0382639, Final residual = 4.8453e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0624202, Final residual = 9.95736e-07, No Iterations 1 +min/max(T) = 797.418, 800.026 +GAMG: Solving for p, Initial residual = 0.115195, Final residual = 0.00730727, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.61157e-08, global = 1.87526e-08, cumulative = 1.45709e-07 +GAMG: Solving for p, Initial residual = 0.00574702, Final residual = 5.24378e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.50586e-08, global = 1.50567e-08, cumulative = 1.60766e-07 +smoothSolver: Solving for epsilon, Initial residual = 0.000641236, Final residual = 2.8365e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0401824, Final residual = 5.01211e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.067274 s +other Time = 0 s +rho Equations = 0.000162 s +U Equations = 0.001335 s +Y Equations = 0.00200132 s +E Equations = 0.00053 s +p Equations = 0.002055 s +calculate parcels = 0.072416 s +chemistry correctThermo = 0.001927 s +turbulence correct = 0.000947 s +combustion correct(in Y) = 0.0581227 s +percentage of chemistry = 86.3969 % +percentage of rho/U/Y/E = 5.98793 % +========Time details of each equation======= +rhoEqn Time = 0.000279 s +rhoEqn assamble = 0.000222 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001334 s +UEqn assamble = 0.000888 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000446 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001396 s +YEqn assamble = 0.000514 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000105 s +YEqn correct boundary = 0 s +EEqn Time = 0.000383 s +EEqn assamble = 0.000289 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 1.3 s ClockTime = 2 s +Courant Number mean: 2.90775e-06 max: 0.000420199 +Time = 4e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 13 new parcels + +Cloud: sprayCloud + Current number of parcels = 140 + Current mass in system = 2.55343e-11 + Linear momentum = (-9.64836e-13 -1.44564e-10 0) + |Linear momentum| = 1.44567e-10 + Linear kinetic energy = 4.62703e-10 + model1: + number of parcels added = 140 + mass introduced = 2.55423e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.248, 405.798 + Mass transfer phase change = 8.03372e-15 + D10, D32, Dmax (mu) = 37.6025, 90.003, 148.262 + Liquid penetration 95% mass (m) = 9.7762e-05 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0999523, Final residual = 1.63033e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.07657, Final residual = 1.67407e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0555017, Final residual = 6.3727e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0397086, Final residual = 4.91459e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0356662, Final residual = 4.53526e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0356662, Final residual = 4.54974e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0554382, Final residual = 9.03529e-07, No Iterations 1 +min/max(T) = 796.72, 800.037 +GAMG: Solving for p, Initial residual = 0.086773, Final residual = 0.0048313, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.49612e-08, global = 2.09041e-08, cumulative = 1.8167e-07 +GAMG: Solving for p, Initial residual = 0.003954, Final residual = 2.87184e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.65717e-08, global = 1.65705e-08, cumulative = 1.98241e-07 +smoothSolver: Solving for epsilon, Initial residual = 0.000628601, Final residual = 2.78099e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0375645, Final residual = 4.68514e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.068312 s +other Time = 0 s +rho Equations = 0.000108 s +U Equations = 0.000955 s +Y Equations = 0.00191701 s +E Equations = 0.00051 s +p Equations = 0.00288 s +calculate parcels = 0.078099 s +chemistry correctThermo = 0.002224 s +turbulence correct = 0.001289 s +combustion correct(in Y) = 0.058237 s +percentage of chemistry = 85.2515 % +percentage of rho/U/Y/E = 5.10893 % +========Time details of each equation======= +rhoEqn Time = 0.000301 s +rhoEqn assamble = 0.000239 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000954 s +UEqn assamble = 0.000562 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000392 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001371 s +YEqn assamble = 0.000501 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000129 s +YEqn correct boundary = 0 s +EEqn Time = 0.000397 s +EEqn assamble = 0.000303 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 1.37 s ClockTime = 2 s +Courant Number mean: 3.58994e-06 max: 0.000459569 +Time = 4.25e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 9 new parcels + +Cloud: sprayCloud + Current number of parcels = 149 + Current mass in system = 2.73e-11 + Linear momentum = (-1.35942e-12 -1.59862e-10 0) + |Linear momentum| = 1.59868e-10 + Linear kinetic energy = 5.30702e-10 + model1: + number of parcels added = 149 + mass introduced = 2.73096e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.228, 410.742 + Mass transfer phase change = 9.615e-15 + D10, D32, Dmax (mu) = 38.5053, 90.2381, 148.269 + Liquid penetration 95% mass (m) = 0.000109629 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0806112, Final residual = 1.38085e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.066811, Final residual = 1.4842e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0498898, Final residual = 5.65689e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.036581, Final residual = 4.48409e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0328973, Final residual = 4.14995e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0328973, Final residual = 4.16329e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0500349, Final residual = 8.20133e-07, No Iterations 1 +min/max(T) = 795.963, 800.05 +GAMG: Solving for p, Initial residual = 0.0754273, Final residual = 0.00353224, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.5044e-08, global = 2.27089e-08, cumulative = 2.2095e-07 +GAMG: Solving for p, Initial residual = 0.00296583, Final residual = 8.03104e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.82301e-08, global = 1.82257e-08, cumulative = 2.39175e-07 +smoothSolver: Solving for epsilon, Initial residual = 0.000616678, Final residual = 2.73007e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0352715, Final residual = 4.39913e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.089105 s +other Time = 0 s +rho Equations = 0.000123 s +U Equations = 0.001101 s +Y Equations = 0.00271458 s +E Equations = 0.000533 s +p Equations = 0.002061 s +calculate parcels = 0.085319 s +chemistry correctThermo = 0.002015 s +turbulence correct = 0.000931 s +combustion correct(in Y) = 0.0794384 s +percentage of chemistry = 89.1515 % +percentage of rho/U/Y/E = 5.01833 % +========Time details of each equation======= +rhoEqn Time = 0.000269 s +rhoEqn assamble = 0.000211 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.0011 s +UEqn assamble = 0.000625 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000475 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002094 s +YEqn assamble = 0.000791 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000258 s +YEqn correct boundary = 0 s +EEqn Time = 0.000403 s +EEqn assamble = 0.000298 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000105 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 1.47 s ClockTime = 2 s +Courant Number mean: 4.25651e-06 max: 0.000497096 +Time = 4.5e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 18 new parcels + +Cloud: sprayCloud + Current number of parcels = 167 + Current mass in system = 3.07685e-11 + Linear momentum = (-8.8896e-13 -1.912e-10 0) + |Linear momentum| = 1.91202e-10 + Linear kinetic energy = 6.75378e-10 + model1: + number of parcels added = 167 + mass introduced = 3.07802e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.204, 415.519 + Mass transfer phase change = 1.17195e-14 + D10, D32, Dmax (mu) = 29.7034, 87.4192, 149.378 + Liquid penetration 95% mass (m) = 0.000122326 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0640852, Final residual = 1.10359e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0606407, Final residual = 1.31437e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0562205, Final residual = 6.31071e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0366952, Final residual = 4.50562e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0309306, Final residual = 3.97016e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0309306, Final residual = 3.98285e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0546777, Final residual = 8.48065e-07, No Iterations 1 +min/max(T) = 794.83, 800.065 +GAMG: Solving for p, Initial residual = 0.0826154, Final residual = 0.00112402, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.08263e-08, global = 2.40128e-08, cumulative = 2.63188e-07 +GAMG: Solving for p, Initial residual = 0.000929639, Final residual = 6.59028e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.42611e-08, global = 2.42566e-08, cumulative = 2.87445e-07 +smoothSolver: Solving for epsilon, Initial residual = 0.000605391, Final residual = 2.68316e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0332455, Final residual = 4.14721e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.096996 s +other Time = 0 s +rho Equations = 0.000113 s +U Equations = 0.001055 s +Y Equations = 0.00203993 s +E Equations = 0.000498 s +p Equations = 0.003077 s +calculate parcels = 0.091941 s +chemistry correctThermo = 0.005267 s +turbulence correct = 0.001121 s +combustion correct(in Y) = 0.0836591 s +percentage of chemistry = 86.25 % +percentage of rho/U/Y/E = 3.8207 % +========Time details of each equation======= +rhoEqn Time = 0.000282 s +rhoEqn assamble = 0.00022 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001054 s +UEqn assamble = 0.000625 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000429 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001474 s +YEqn assamble = 0.000514 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000198 s +YEqn correct boundary = 0 s +EEqn Time = 0.000377 s +EEqn assamble = 0.000281 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 1.57 s ClockTime = 2 s +Courant Number mean: 5.20005e-06 max: 0.000712165 +Time = 4.75e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 15 new parcels + +Cloud: sprayCloud + Current number of parcels = 182 + Current mass in system = 3.36273e-11 + Linear momentum = (-9.30584e-13 -2.17577e-10 0) + |Linear momentum| = 2.17579e-10 + Linear kinetic energy = 8.00239e-10 + model1: + number of parcels added = 182 + mass introduced = 3.36413e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.219, 420.141 + Mass transfer phase change = 1.40592e-14 + D10, D32, Dmax (mu) = 30.7595, 87.5994, 149.359 + Liquid penetration 95% mass (m) = 0.000135226 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0722075, Final residual = 9.18595e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0617665, Final residual = 1.29368e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0508295, Final residual = 5.62883e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0343893, Final residual = 4.18226e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0290564, Final residual = 3.70646e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0290565, Final residual = 3.71838e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0507884, Final residual = 7.99352e-07, No Iterations 1 +min/max(T) = 793.599, 800.081 +GAMG: Solving for p, Initial residual = 0.0745621, Final residual = 0.00394459, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.47496e-08, global = 3.36993e-08, cumulative = 3.21144e-07 +GAMG: Solving for p, Initial residual = 0.00334613, Final residual = 1.76467e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.69685e-08, global = 2.6967e-08, cumulative = 3.48111e-07 +smoothSolver: Solving for epsilon, Initial residual = 0.000594674, Final residual = 2.63985e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.031442, Final residual = 3.92342e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.073539 s +other Time = 0 s +rho Equations = 0.000117 s +U Equations = 0.001119 s +Y Equations = 0.0023786 s +E Equations = 0.000592 s +p Equations = 0.002577 s +calculate parcels = 0.100823 s +chemistry correctThermo = 0.00276 s +turbulence correct = 0.001037 s +combustion correct(in Y) = 0.0628074 s +percentage of chemistry = 85.4069 % +percentage of rho/U/Y/E = 5.72023 % +========Time details of each equation======= +rhoEqn Time = 0.000262 s +rhoEqn assamble = 0.000204 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001117 s +UEqn assamble = 0.000591 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000526 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001689 s +YEqn assamble = 0.000655 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000159 s +YEqn correct boundary = 0 s +EEqn Time = 0.000438 s +EEqn assamble = 0.000325 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 1.65 s ClockTime = 2 s +Courant Number mean: 6.21311e-06 max: 0.00080712 +Time = 5e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 16 new parcels + +Cloud: sprayCloud + Current number of parcels = 198 + Current mass in system = 3.66349e-11 + Linear momentum = (-1.65353e-12 -2.46035e-10 0) + |Linear momentum| = 2.46041e-10 + Linear kinetic energy = 9.39253e-10 + model1: + number of parcels added = 198 + mass introduced = 3.66516e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.226, 424.612 + Mass transfer phase change = 1.66497e-14 + D10, D32, Dmax (mu) = 31.8576, 88.0168, 149.346 + Liquid penetration 95% mass (m) = 0.000148589 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0662595, Final residual = 8.36391e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0602453, Final residual = 1.25628e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0466971, Final residual = 5.11841e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0325926, Final residual = 3.98314e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0276584, Final residual = 3.58499e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0276585, Final residual = 3.59647e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0466408, Final residual = 7.55568e-07, No Iterations 1 +min/max(T) = 792.288, 800.101 +GAMG: Solving for p, Initial residual = 0.0687588, Final residual = 0.0031519, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.77235e-08, global = 3.45261e-08, cumulative = 3.82637e-07 +GAMG: Solving for p, Initial residual = 0.00268678, Final residual = 2.54786e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.98603e-08, global = 2.98577e-08, cumulative = 4.12495e-07 +smoothSolver: Solving for epsilon, Initial residual = 0.000584466, Final residual = 2.59969e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0298009, Final residual = 3.71994e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.102792 s +other Time = 0 s +rho Equations = 8.7e-05 s +U Equations = 0.000873 s +Y Equations = 0.0022893 s +E Equations = 0.000587 s +p Equations = 0.002464 s +calculate parcels = 0.108172 s +chemistry correctThermo = 0.002737 s +turbulence correct = 0.001038 s +combustion correct(in Y) = 0.0925867 s +percentage of chemistry = 90.0719 % +percentage of rho/U/Y/E = 3.7321 % +========Time details of each equation======= +rhoEqn Time = 0.000222 s +rhoEqn assamble = 0.000174 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 4.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000873 s +UEqn assamble = 0.000474 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000399 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001778 s +YEqn assamble = 0.000608 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000241 s +YEqn correct boundary = 0 s +EEqn Time = 0.000436 s +EEqn assamble = 0.000325 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 1.76 s ClockTime = 2 s +Courant Number mean: 7.24096e-06 max: 0.00086796 +Time = 5.25e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 15 new parcels + +Cloud: sprayCloud + Current number of parcels = 213 + Current mass in system = 3.94216e-11 + Linear momentum = (-2.18761e-12 -2.73154e-10 0) + |Linear momentum| = 2.73163e-10 + Linear kinetic energy = 1.07513e-09 + model1: + number of parcels added = 213 + mass introduced = 3.94412e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.236, 428.938 + Mass transfer phase change = 1.95694e-14 + D10, D32, Dmax (mu) = 32.6463, 87.294, 149.342 + Liquid penetration 95% mass (m) = 0.000162644 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0561778, Final residual = 7.60876e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0561424, Final residual = 1.19126e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0443318, Final residual = 4.80753e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0311364, Final residual = 3.78539e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0261724, Final residual = 3.39908e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0261725, Final residual = 3.40999e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0439653, Final residual = 7.21072e-07, No Iterations 1 +min/max(T) = 790.829, 800.126 +GAMG: Solving for p, Initial residual = 0.0614852, Final residual = 0.00207736, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.56188e-08, global = 3.67969e-08, cumulative = 4.49292e-07 +GAMG: Solving for p, Initial residual = 0.00179955, Final residual = 7.238e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.36615e-08, global = 3.36529e-08, cumulative = 4.82945e-07 +smoothSolver: Solving for epsilon, Initial residual = 0.000575134, Final residual = 2.56163e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0283235, Final residual = 3.53697e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.100365 s +other Time = 0 s +rho Equations = 0.000114 s +U Equations = 0.000985 s +Y Equations = 0.00250089 s +E Equations = 0.000638 s +p Equations = 0.002527 s +calculate parcels = 0.117096 s +chemistry correctThermo = 0.002741 s +turbulence correct = 0.001049 s +combustion correct(in Y) = 0.0896671 s +percentage of chemistry = 89.341 % +percentage of rho/U/Y/E = 4.22248 % +========Time details of each equation======= +rhoEqn Time = 0.000265 s +rhoEqn assamble = 0.000203 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000983 s +UEqn assamble = 0.000524 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000459 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001921 s +YEqn assamble = 0.000697 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00025 s +YEqn correct boundary = 0 s +EEqn Time = 0.000472 s +EEqn assamble = 0.000354 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 1.87 s ClockTime = 2 s +Courant Number mean: 8.32694e-06 max: 0.000961133 +Time = 5.5e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 20 new parcels + +Cloud: sprayCloud + Current number of parcels = 233 + Current mass in system = 4.30935e-11 + Linear momentum = (-2.43016e-12 -3.09963e-10 0) + |Linear momentum| = 3.09972e-10 + Linear kinetic energy = 1.26496e-09 + model1: + number of parcels added = 233 + mass introduced = 4.31165e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.242, 433.119 + Mass transfer phase change = 2.29642e-14 + D10, D32, Dmax (mu) = 33.1748, 86.6249, 149.346 + Liquid penetration 95% mass (m) = 0.000176817 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.050006, Final residual = 6.80205e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0527129, Final residual = 1.12491e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0438507, Final residual = 4.71341e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0304589, Final residual = 3.72041e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0250795, Final residual = 3.32637e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0250795, Final residual = 3.33697e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0434888, Final residual = 7.06852e-07, No Iterations 1 +min/max(T) = 789.098, 800.156 +GAMG: Solving for p, Initial residual = 0.0585792, Final residual = 0.00254138, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.08056e-08, global = 4.53632e-08, cumulative = 5.28308e-07 +GAMG: Solving for p, Initial residual = 0.00223465, Final residual = 9.56923e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.91417e-08, global = 3.91284e-08, cumulative = 5.67436e-07 +smoothSolver: Solving for epsilon, Initial residual = 0.000565901, Final residual = 2.52377e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0269858, Final residual = 3.37165e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.08715 s +other Time = 0 s +rho Equations = 0.000143 s +U Equations = 0.001242 s +Y Equations = 0.00209584 s +E Equations = 0.000531 s +p Equations = 0.001892 s +calculate parcels = 0.126682 s +chemistry correctThermo = 0.001953 s +turbulence correct = 0.000852 s +combustion correct(in Y) = 0.0782852 s +percentage of chemistry = 89.8281 % +percentage of rho/U/Y/E = 4.60337 % +========Time details of each equation======= +rhoEqn Time = 0.000257 s +rhoEqn assamble = 0.000201 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001241 s +UEqn assamble = 0.000731 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00051 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001289 s +YEqn assamble = 0.000529 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 7e-06 s +YEqn correct boundary = 0 s +EEqn Time = 0.000381 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 1.97 s ClockTime = 2 s +Courant Number mean: 9.60764e-06 max: 0.00114098 +Time = 5.75e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 19 new parcels + +Cloud: sprayCloud + Current number of parcels = 252 + Current mass in system = 4.65614e-11 + Linear momentum = (-1.63994e-12 -3.45587e-10 0) + |Linear momentum| = 3.45591e-10 + Linear kinetic energy = 1.4527e-09 + model1: + number of parcels added = 252 + mass introduced = 4.6588e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.22, 437.16 + Mass transfer phase change = 2.6669e-14 + D10, D32, Dmax (mu) = 34.1828, 86.8423, 149.359 + Liquid penetration 95% mass (m) = 0.000192375 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0515551, Final residual = 6.37302e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0510786, Final residual = 1.08725e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0405485, Final residual = 4.3555e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0288613, Final residual = 3.53588e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0238182, Final residual = 3.18661e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0238183, Final residual = 3.19675e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0407415, Final residual = 6.74542e-07, No Iterations 1 +min/max(T) = 787.254, 800.19 +GAMG: Solving for p, Initial residual = 0.0542914, Final residual = 0.00114443, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.90772e-08, global = 4.54072e-08, cumulative = 6.12843e-07 +GAMG: Solving for p, Initial residual = 0.00100829, Final residual = 2.74387e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.27062e-08, global = 4.27018e-08, cumulative = 6.55545e-07 +smoothSolver: Solving for epsilon, Initial residual = 0.000556861, Final residual = 2.4873e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0257694, Final residual = 3.2215e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.079281 s +other Time = 0 s +rho Equations = 9e-05 s +U Equations = 0.000864 s +Y Equations = 0.00224762 s +E Equations = 0.0006 s +p Equations = 0.00193 s +calculate parcels = 0.134731 s +chemistry correctThermo = 0.002746 s +turbulence correct = 0.00084 s +combustion correct(in Y) = 0.0698254 s +percentage of chemistry = 88.0733 % +percentage of rho/U/Y/E = 4.79512 % +========Time details of each equation======= +rhoEqn Time = 0.0002 s +rhoEqn assamble = 0.000158 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 4.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000863 s +UEqn assamble = 0.000474 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000389 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001689 s +YEqn assamble = 0.000616 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000214 s +YEqn correct boundary = 0 s +EEqn Time = 0.000436 s +EEqn assamble = 0.000327 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000109 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 2.06 s ClockTime = 2 s +Courant Number mean: 1.09747e-05 max: 0.0012777 +Time = 6e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 28 new parcels + +Cloud: sprayCloud + Current number of parcels = 280 + Current mass in system = 5.16403e-11 + Linear momentum = (-5.37365e-13 -3.99798e-10 0) + |Linear momentum| = 3.99798e-10 + Linear kinetic energy = 1.74853e-09 + model1: + number of parcels added = 280 + mass introduced = 5.16711e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.214, 441.062 + Mass transfer phase change = 3.08181e-14 + D10, D32, Dmax (mu) = 35.4434, 87.3792, 149.517 + Liquid penetration 95% mass (m) = 0.000208161 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0482959, Final residual = 6.1807e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0490859, Final residual = 1.0414e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0390386, Final residual = 4.30732e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0280645, Final residual = 3.56508e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0230441, Final residual = 3.23742e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0230442, Final residual = 3.24748e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0394198, Final residual = 6.65669e-07, No Iterations 1 +min/max(T) = 785.187, 800.232 +GAMG: Solving for p, Initial residual = 0.0526521, Final residual = 0.00112658, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.67817e-08, global = 5.14133e-08, cumulative = 7.06959e-07 +GAMG: Solving for p, Initial residual = 0.00100668, Final residual = 2.9391e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.7828e-08, global = 4.78225e-08, cumulative = 7.54781e-07 +smoothSolver: Solving for epsilon, Initial residual = 0.000548231, Final residual = 2.45308e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0246581, Final residual = 3.08451e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.092083 s +other Time = 1e-06 s +rho Equations = 7.4e-05 s +U Equations = 0.000968 s +Y Equations = 0.00235797 s +E Equations = 0.000591 s +p Equations = 0.002405 s +calculate parcels = 0.143171 s +chemistry correctThermo = 0.002721 s +turbulence correct = 0.001063 s +combustion correct(in Y) = 0.081786 s +percentage of chemistry = 88.8177 % +percentage of rho/U/Y/E = 4.3341 % +========Time details of each equation======= +rhoEqn Time = 0.000218 s +rhoEqn assamble = 0.00017 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 4.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000968 s +UEqn assamble = 0.000444 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000524 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001719 s +YEqn assamble = 0.000633 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000176 s +YEqn correct boundary = 0 s +EEqn Time = 0.00044 s +EEqn assamble = 0.000329 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 2.16 s ClockTime = 3 s +Courant Number mean: 1.24899e-05 max: 0.00145946 +Time = 6.25e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 18 new parcels + +Cloud: sprayCloud + Current number of parcels = 298 + Current mass in system = 5.49138e-11 + Linear momentum = (1.61004e-12 -4.34666e-10 0) + |Linear momentum| = 4.34669e-10 + Linear kinetic energy = 1.94041e-09 + model1: + number of parcels added = 298 + mass introduced = 5.49491e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.241, 444.825 + Mass transfer phase change = 3.52754e-14 + D10, D32, Dmax (mu) = 36.2903, 87.4458, 149.306 + Liquid penetration 95% mass (m) = 0.000224445 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.047572, Final residual = 5.98868e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0471706, Final residual = 1.00412e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.036097, Final residual = 4.06999e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0266265, Final residual = 3.45954e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0220156, Final residual = 3.17439e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0220157, Final residual = 3.18413e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0367413, Final residual = 6.39087e-07, No Iterations 1 +min/max(T) = 783.031, 800.281 +GAMG: Solving for p, Initial residual = 0.0490943, Final residual = 0.000877093, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.82948e-08, global = 5.42635e-08, cumulative = 8.09045e-07 +GAMG: Solving for p, Initial residual = 0.000784768, Final residual = 3.96249e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.1383e-08, global = 5.13747e-08, cumulative = 8.60419e-07 +smoothSolver: Solving for epsilon, Initial residual = 0.000539995, Final residual = 2.42101e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0236392, Final residual = 2.95901e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.093473 s +other Time = 0 s +rho Equations = 0.000109 s +U Equations = 0.001028 s +Y Equations = 0.00229334 s +E Equations = 0.000589 s +p Equations = 0.002337 s +calculate parcels = 0.154149 s +chemistry correctThermo = 0.00275 s +turbulence correct = 0.001066 s +combustion correct(in Y) = 0.0831557 s +percentage of chemistry = 88.9622 % +percentage of rho/U/Y/E = 4.3 % +========Time details of each equation======= +rhoEqn Time = 0.000249 s +rhoEqn assamble = 0.000195 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001028 s +UEqn assamble = 0.000559 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000469 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001677 s +YEqn assamble = 0.000611 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00019 s +YEqn correct boundary = 0 s +EEqn Time = 0.000437 s +EEqn assamble = 0.000327 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00011 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 2.26 s ClockTime = 3 s +Courant Number mean: 1.40636e-05 max: 0.00160338 +Time = 6.5e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 18 new parcels + +Cloud: sprayCloud + Current number of parcels = 316 + Current mass in system = 5.81641e-11 + Linear momentum = (1.63328e-12 -4.70174e-10 0) + |Linear momentum| = 4.70177e-10 + Linear kinetic energy = 2.14043e-09 + model1: + number of parcels added = 316 + mass introduced = 5.82042e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.243, 448.451 + Mass transfer phase change = 4.00777e-14 + D10, D32, Dmax (mu) = 36.9953, 87.6685, 149.106 + Liquid penetration 95% mass (m) = 0.000241542 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0426971, Final residual = 5.71199e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0447442, Final residual = 9.56085e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0338746, Final residual = 3.98942e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0256048, Final residual = 3.49359e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0213722, Final residual = 3.25637e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0213723, Final residual = 3.26609e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0344729, Final residual = 6.20813e-07, No Iterations 1 +min/max(T) = 780.766, 800.341 +GAMG: Solving for p, Initial residual = 0.0449985, Final residual = 0.000830794, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.34686e-08, global = 6.00359e-08, cumulative = 9.20455e-07 +GAMG: Solving for p, Initial residual = 0.000749084, Final residual = 3.2084e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.53583e-08, global = 5.53507e-08, cumulative = 9.75806e-07 +smoothSolver: Solving for epsilon, Initial residual = 0.00053209, Final residual = 2.39068e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0227017, Final residual = 2.84358e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.091287 s +other Time = 0 s +rho Equations = 0.000108 s +U Equations = 0.001038 s +Y Equations = 0.00232345 s +E Equations = 0.000604 s +p Equations = 0.002415 s +calculate parcels = 0.16544 s +chemistry correctThermo = 0.002758 s +turbulence correct = 0.0011 s +combustion correct(in Y) = 0.0807955 s +percentage of chemistry = 88.5072 % +percentage of rho/U/Y/E = 4.46225 % +========Time details of each equation======= +rhoEqn Time = 0.00027 s +rhoEqn assamble = 0.000211 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001037 s +UEqn assamble = 0.000559 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000478 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001704 s +YEqn assamble = 0.000638 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000189 s +YEqn correct boundary = 0 s +EEqn Time = 0.000449 s +EEqn assamble = 0.000334 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 2.36 s ClockTime = 3 s +Courant Number mean: 1.56284e-05 max: 0.00172823 +Time = 6.75e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 32 new parcels + +Cloud: sprayCloud + Current number of parcels = 348 + Current mass in system = 6.39072e-11 + Linear momentum = (2.32649e-12 -5.35863e-10 0) + |Linear momentum| = 5.35868e-10 + Linear kinetic energy = 2.5256e-09 + model1: + number of parcels added = 348 + mass introduced = 6.39526e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.228, 451.936 + Mass transfer phase change = 4.53911e-14 + D10, D32, Dmax (mu) = 38.3013, 88.3478, 148.917 + Liquid penetration 95% mass (m) = 0.000258755 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0369153, Final residual = 5.14586e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0424025, Final residual = 9.04716e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0329604, Final residual = 3.98475e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0248822, Final residual = 3.47205e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0205413, Final residual = 3.21315e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0205414, Final residual = 3.22263e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0337877, Final residual = 6.1259e-07, No Iterations 1 +min/max(T) = 778.231, 800.41 +GAMG: Solving for p, Initial residual = 0.0447625, Final residual = 0.00124841, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.17811e-08, global = 6.70198e-08, cumulative = 1.04283e-06 +GAMG: Solving for p, Initial residual = 0.00114306, Final residual = 4.8876e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.12549e-08, global = 6.1242e-08, cumulative = 1.10407e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000524515, Final residual = 2.36206e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0218414, Final residual = 2.73701e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.088421 s +other Time = 1e-06 s +rho Equations = 9.7e-05 s +U Equations = 0.001034 s +Y Equations = 0.00232728 s +E Equations = 0.000631 s +p Equations = 0.002436 s +calculate parcels = 0.177575 s +chemistry correctThermo = 0.002769 s +turbulence correct = 0.001031 s +combustion correct(in Y) = 0.0779497 s +percentage of chemistry = 88.1575 % +percentage of rho/U/Y/E = 4.62479 % +========Time details of each equation======= +rhoEqn Time = 0.000249 s +rhoEqn assamble = 0.000192 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001034 s +UEqn assamble = 0.000556 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000478 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001707 s +YEqn assamble = 0.000627 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000186 s +YEqn correct boundary = 0 s +EEqn Time = 0.000451 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 2.47 s ClockTime = 3 s +Courant Number mean: 1.73434e-05 max: 0.0019476 +Time = 7e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 31 new parcels + +Cloud: sprayCloud + Current number of parcels = 379 + Current mass in system = 6.95089e-11 + Linear momentum = (2.13877e-12 -6.00998e-10 0) + |Linear momentum| = 6.01001e-10 + Linear kinetic energy = 2.91466e-09 + model1: + number of parcels added = 379 + mass introduced = 6.95602e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.216, 455.283 + Mass transfer phase change = 5.13149e-14 + D10, D32, Dmax (mu) = 39.3597, 87.3591, 149.479 + Liquid penetration 95% mass (m) = 0.000277236 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0364849, Final residual = 4.58857e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.041268, Final residual = 8.68786e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0324345, Final residual = 4.05094e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0242129, Final residual = 3.47903e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0195927, Final residual = 3.17592e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0195928, Final residual = 3.18511e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0337351, Final residual = 6.15393e-07, No Iterations 1 +min/max(T) = 775.355, 800.479 +GAMG: Solving for p, Initial residual = 0.0438023, Final residual = 0.00183181, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.18397e-07, global = 8.45968e-08, cumulative = 1.18866e-06 +GAMG: Solving for p, Initial residual = 0.001676, Final residual = 6.87205e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.82979e-08, global = 6.82776e-08, cumulative = 1.25694e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000517248, Final residual = 2.33504e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0210508, Final residual = 2.63843e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.092213 s +other Time = 0 s +rho Equations = 0.000141 s +U Equations = 0.001114 s +Y Equations = 0.00204211 s +E Equations = 0.000484 s +p Equations = 0.001913 s +calculate parcels = 0.190344 s +chemistry correctThermo = 0.00195 s +turbulence correct = 0.000835 s +combustion correct(in Y) = 0.0835779 s +percentage of chemistry = 90.6357 % +percentage of rho/U/Y/E = 4.10041 % +========Time details of each equation======= +rhoEqn Time = 0.000263 s +rhoEqn assamble = 0.000207 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001114 s +UEqn assamble = 0.000634 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00048 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001403 s +YEqn assamble = 0.00051 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00014 s +YEqn correct boundary = 0 s +EEqn Time = 0.000367 s +EEqn assamble = 0.000271 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 2.57 s ClockTime = 3 s +Courant Number mean: 1.93266e-05 max: 0.00222116 +Time = 7.25e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 21 new parcels + +Cloud: sprayCloud + Current number of parcels = 400 + Current mass in system = 7.33231e-11 + Linear momentum = (1.87883e-12 -6.45364e-10 0) + |Linear momentum| = 6.45367e-10 + Linear kinetic energy = 3.18191e-09 + model1: + number of parcels added = 400 + mass introduced = 7.33808e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.231, 458.491 + Mass transfer phase change = 5.76322e-14 + D10, D32, Dmax (mu) = 40.0466, 86.7652, 149.145 + Liquid penetration 95% mass (m) = 0.00029596 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.039959, Final residual = 4.41546e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.041041, Final residual = 8.5741e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0304491, Final residual = 3.90356e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0229882, Final residual = 3.38127e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0185847, Final residual = 3.08993e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0185849, Final residual = 3.09876e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0320649, Final residual = 6.0127e-07, No Iterations 1 +min/max(T) = 772.368, 800.549 +GAMG: Solving for p, Initial residual = 0.0434308, Final residual = 0.000977221, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.02047e-07, global = 7.77985e-08, cumulative = 1.33474e-06 +GAMG: Solving for p, Initial residual = 0.000893965, Final residual = 3.29295e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.28246e-08, global = 7.2814e-08, cumulative = 1.40755e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000510298, Final residual = 2.30975e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0203143, Final residual = 2.54733e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.082982 s +other Time = 1e-06 s +rho Equations = 8.9e-05 s +U Equations = 0.000887 s +Y Equations = 0.00219268 s +E Equations = 0.0006 s +p Equations = 0.003194 s +calculate parcels = 0.202871 s +chemistry correctThermo = 0.003046 s +turbulence correct = 0.001362 s +combustion correct(in Y) = 0.0714603 s +percentage of chemistry = 86.1154 % +percentage of rho/U/Y/E = 4.54156 % +========Time details of each equation======= +rhoEqn Time = 0.000309 s +rhoEqn assamble = 0.000251 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000885 s +UEqn assamble = 0.000459 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000426 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001653 s +YEqn assamble = 0.00061 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000209 s +YEqn correct boundary = 0 s +EEqn Time = 0.00044 s +EEqn assamble = 0.000326 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 2.67 s ClockTime = 3 s +Courant Number mean: 2.144e-05 max: 0.00242783 +Time = 7.5e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 23 new parcels + +Cloud: sprayCloud + Current number of parcels = 423 + Current mass in system = 7.74856e-11 + Linear momentum = (2.74652e-12 -6.94855e-10 0) + |Linear momentum| = 6.9486e-10 + Linear kinetic energy = 3.48679e-09 + model1: + number of parcels added = 423 + mass introduced = 7.755e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.247, 461.558 + Mass transfer phase change = 6.43906e-14 + D10, D32, Dmax (mu) = 40.8427, 86.8385, 148.827 + Liquid penetration 95% mass (m) = 0.000314859 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0384324, Final residual = 4.47481e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0402274, Final residual = 8.41608e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0289565, Final residual = 3.94496e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0221139, Final residual = 3.42958e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0179106, Final residual = 3.12709e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0179108, Final residual = 3.13578e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0305819, Final residual = 6.00865e-07, No Iterations 1 +min/max(T) = 769.238, 800.631 +GAMG: Solving for p, Initial residual = 0.040831, Final residual = 0.000831778, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.06024e-07, global = 8.21408e-08, cumulative = 1.4897e-06 +GAMG: Solving for p, Initial residual = 0.000754433, Final residual = 3.73025e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.79108e-08, global = 7.78974e-08, cumulative = 1.56759e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000503608, Final residual = 2.28582e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0196291, Final residual = 2.46285e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.07366 s +other Time = 0 s +rho Equations = 0.000119 s +U Equations = 0.001042 s +Y Equations = 0.00195322 s +E Equations = 0.000489 s +p Equations = 0.001874 s +calculate parcels = 0.216932 s +chemistry correctThermo = 0.001976 s +turbulence correct = 0.001191 s +combustion correct(in Y) = 0.0648658 s +percentage of chemistry = 88.0611 % +percentage of rho/U/Y/E = 4.89169 % +========Time details of each equation======= +rhoEqn Time = 0.000233 s +rhoEqn assamble = 0.000181 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001042 s +UEqn assamble = 0.00057 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000472 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001349 s +YEqn assamble = 0.000505 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000372 s +EEqn assamble = 0.000279 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 2.74 s ClockTime = 3 s +Courant Number mean: 2.36362e-05 max: 0.00262678 +Time = 7.75e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 20 new parcels + +Cloud: sprayCloud + Current number of parcels = 443 + Current mass in system = 8.10977e-11 + Linear momentum = (1.68753e-12 -7.37907e-10 0) + |Linear momentum| = 7.37909e-10 + Linear kinetic energy = 3.75487e-09 + model1: + number of parcels added = 443 + mass introduced = 8.11692e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.299, 464.482 + Mass transfer phase change = 7.15682e-14 + D10, D32, Dmax (mu) = 41.3368, 86.8027, 148.521 + Liquid penetration 95% mass (m) = 0.000334455 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0360032, Final residual = 4.4382e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0388323, Final residual = 8.20941e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0274482, Final residual = 3.94288e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0211088, Final residual = 3.40933e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0170374, Final residual = 3.07413e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0170375, Final residual = 3.08251e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0290462, Final residual = 5.94522e-07, No Iterations 1 +min/max(T) = 765.986, 800.719 +GAMG: Solving for p, Initial residual = 0.0387672, Final residual = 0.000696159, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.08672e-07, global = 8.6753e-08, cumulative = 1.65435e-06 +GAMG: Solving for p, Initial residual = 0.000633114, Final residual = 2.72837e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.27389e-08, global = 8.27281e-08, cumulative = 1.73707e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000497185, Final residual = 2.26324e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0189899, Final residual = 2.38416e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.104437 s +other Time = 0 s +rho Equations = 9.2e-05 s +U Equations = 0.000867 s +Y Equations = 0.00228796 s +E Equations = 0.000486 s +p Equations = 0.001879 s +calculate parcels = 0.230061 s +chemistry correctThermo = 0.001969 s +turbulence correct = 0.00086 s +combustion correct(in Y) = 0.095869 s +percentage of chemistry = 91.7961 % +percentage of rho/U/Y/E = 3.57436 % +========Time details of each equation======= +rhoEqn Time = 0.000207 s +rhoEqn assamble = 0.000162 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 4.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000865 s +UEqn assamble = 0.000474 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000391 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001197 s +YEqn assamble = 0.000538 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -0.000127 s +YEqn correct boundary = 0 s +EEqn Time = 0.000364 s +EEqn assamble = 0.000272 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 2.87 s ClockTime = 3 s +Courant Number mean: 2.58964e-05 max: 0.00283069 +Time = 8e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 30 new parcels + +Cloud: sprayCloud + Current number of parcels = 473 + Current mass in system = 8.64961e-11 + Linear momentum = (1.41121e-12 -8.05752e-10 0) + |Linear momentum| = 8.05753e-10 + Linear kinetic energy = 4.1962e-09 + model1: + number of parcels added = 473 + mass introduced = 8.65754e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.274, 467.264 + Mass transfer phase change = 7.92381e-14 + D10, D32, Dmax (mu) = 42.2452, 86.8306, 148.37 + Liquid penetration 95% mass (m) = 0.000353452 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0335228, Final residual = 4.24596e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0373962, Final residual = 7.94586e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0263555, Final residual = 4.03262e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0204144, Final residual = 3.47912e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0164574, Final residual = 3.10852e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0164575, Final residual = 3.11678e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0280042, Final residual = 5.95591e-07, No Iterations 1 +min/max(T) = 762.547, 800.812 +GAMG: Solving for p, Initial residual = 0.03763, Final residual = 0.000676115, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.15995e-07, global = 9.16538e-08, cumulative = 1.82873e-06 +GAMG: Solving for p, Initial residual = 0.000623399, Final residual = 1.99221e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.84124e-08, global = 8.84037e-08, cumulative = 1.91713e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000490999, Final residual = 2.24182e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0183935, Final residual = 2.311e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.099568 s +other Time = 0 s +rho Equations = 9.9e-05 s +U Equations = 0.000889 s +Y Equations = 0.00229654 s +E Equations = 0.000601 s +p Equations = 0.002359 s +calculate parcels = 0.243134 s +chemistry correctThermo = 0.002697 s +turbulence correct = 0.001006 s +combustion correct(in Y) = 0.0894865 s +percentage of chemistry = 89.8747 % +percentage of rho/U/Y/E = 3.90239 % +========Time details of each equation======= +rhoEqn Time = 0.000246 s +rhoEqn assamble = 0.000193 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000888 s +UEqn assamble = 0.000492 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000396 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001726 s +YEqn assamble = 0.000641 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000206 s +YEqn correct boundary = 0 s +EEqn Time = 0.00044 s +EEqn assamble = 0.000326 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 2.98 s ClockTime = 3 s +Courant Number mean: 2.82588e-05 max: 0.00306911 +Time = 8.25e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 23 new parcels + +Cloud: sprayCloud + Current number of parcels = 496 + Current mass in system = 9.06513e-11 + Linear momentum = (1.78579e-12 -8.5777e-10 0) + |Linear momentum| = 8.57772e-10 + Linear kinetic energy = 4.53744e-09 + model1: + number of parcels added = 496 + mass introduced = 9.07385e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.237, 469.903 + Mass transfer phase change = 8.72693e-14 + D10, D32, Dmax (mu) = 42.8723, 87.1768, 149.349 + Liquid penetration 95% mass (m) = 0.000373935 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0319215, Final residual = 3.90225e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0361251, Final residual = 7.68136e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0248247, Final residual = 4.0238e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.019447, Final residual = 3.46596e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0157206, Final residual = 3.06339e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0157208, Final residual = 3.07135e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0264682, Final residual = 5.85769e-07, No Iterations 1 +min/max(T) = 759.05, 800.907 +GAMG: Solving for p, Initial residual = 0.0358627, Final residual = 0.000506455, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.14953e-07, global = 9.6112e-08, cumulative = 2.01324e-06 +GAMG: Solving for p, Initial residual = 0.000469704, Final residual = 8.61768e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.26077e-08, global = 9.25671e-08, cumulative = 2.10581e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000485059, Final residual = 2.22161e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0178335, Final residual = 2.2425e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.079007 s +other Time = 0 s +rho Equations = 0.000135 s +U Equations = 0.001103 s +Y Equations = 0.00230668 s +E Equations = 0.000588 s +p Equations = 0.002206 s +calculate parcels = 0.256527 s +chemistry correctThermo = 0.002817 s +turbulence correct = 0.001007 s +combustion correct(in Y) = 0.0686363 s +percentage of chemistry = 86.8737 % +percentage of rho/U/Y/E = 5.23078 % +========Time details of each equation======= +rhoEqn Time = 0.000293 s +rhoEqn assamble = 0.000229 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001102 s +UEqn assamble = 0.000617 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000485 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00166 s +YEqn assamble = 0.000621 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000163 s +YEqn correct boundary = 0 s +EEqn Time = 0.000435 s +EEqn assamble = 0.000323 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 3.08 s ClockTime = 3 s +Courant Number mean: 3.06246e-05 max: 0.00327174 +Time = 8.5e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 31 new parcels + +Cloud: sprayCloud + Current number of parcels = 527 + Current mass in system = 9.62199e-11 + Linear momentum = (3.97533e-12 -9.29938e-10 0) + |Linear momentum| = 9.29946e-10 + Linear kinetic energy = 5.02304e-09 + model1: + number of parcels added = 527 + mass introduced = 9.63158e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.253, 472.894 + Mass transfer phase change = 9.58953e-14 + D10, D32, Dmax (mu) = 43.5483, 86.9765, 149.056 + Liquid penetration 95% mass (m) = 0.000392882 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0282924, Final residual = 3.44972e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0348894, Final residual = 7.38619e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.024213, Final residual = 4.2114e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0189625, Final residual = 3.57702e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.015206, Final residual = 3.08853e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0152062, Final residual = 3.09634e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0259459, Final residual = 5.95946e-07, No Iterations 1 +min/max(T) = 755.294, 801.009 +GAMG: Solving for p, Initial residual = 0.0353187, Final residual = 0.000809479, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.38393e-07, global = 1.06513e-07, cumulative = 2.21232e-06 +GAMG: Solving for p, Initial residual = 0.000753724, Final residual = 2.83506e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.94371e-08, global = 9.94227e-08, cumulative = 2.31175e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000479328, Final residual = 2.2024e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0173107, Final residual = 2.17846e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.079361 s +other Time = 0 s +rho Equations = 0.000104 s +U Equations = 0.001112 s +Y Equations = 0.00198876 s +E Equations = 0.000486 s +p Equations = 0.001873 s +calculate parcels = 0.272412 s +chemistry correctThermo = 0.001971 s +turbulence correct = 0.000861 s +combustion correct(in Y) = 0.0708272 s +percentage of chemistry = 89.2469 % +percentage of rho/U/Y/E = 4.6506 % +========Time details of each equation======= +rhoEqn Time = 0.000219 s +rhoEqn assamble = 0.000169 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001111 s +UEqn assamble = 0.000635 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000476 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001381 s +YEqn assamble = 0.000517 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000103 s +YEqn correct boundary = 0 s +EEqn Time = 0.000368 s +EEqn assamble = 0.000276 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 3.17 s ClockTime = 4 s +Courant Number mean: 3.31341e-05 max: 0.00355797 +Time = 8.75e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 17 new parcels + +Cloud: sprayCloud + Current number of parcels = 544 + Current mass in system = 9.92273e-11 + Linear momentum = (3.62e-12 -9.66344e-10 0) + |Linear momentum| = 9.66351e-10 + Linear kinetic energy = 5.25591e-09 + model1: + number of parcels added = 544 + mass introduced = 9.93322e-11 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.238, 476.235 + Mass transfer phase change = 1.0487e-13 + D10, D32, Dmax (mu) = 43.717, 86.7489, 148.616 + Liquid penetration 95% mass (m) = 0.000412788 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0275523, Final residual = 2.98281e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0339692, Final residual = 7.17005e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0228018, Final residual = 4.19477e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0180755, Final residual = 3.56405e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0145705, Final residual = 3.03602e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0145707, Final residual = 3.04354e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0245596, Final residual = 5.86486e-07, No Iterations 1 +min/max(T) = 751.517, 801.111 +GAMG: Solving for p, Initial residual = 0.03437, Final residual = 0.000541654, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.30941e-07, global = 1.06337e-07, cumulative = 2.41808e-06 +GAMG: Solving for p, Initial residual = 0.000505966, Final residual = 2.05636e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.03452e-07, global = 1.03441e-07, cumulative = 2.52152e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000473819, Final residual = 2.18434e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0168173, Final residual = 2.11836e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.072684 s +other Time = 0 s +rho Equations = 0.00011 s +U Equations = 0.001085 s +Y Equations = 0.00197962 s +E Equations = 0.000473 s +p Equations = 0.001841 s +calculate parcels = 0.288292 s +chemistry correctThermo = 0.001979 s +turbulence correct = 0.000886 s +combustion correct(in Y) = 0.0641834 s +percentage of chemistry = 88.3047 % +percentage of rho/U/Y/E = 5.01847 % +========Time details of each equation======= +rhoEqn Time = 0.00022 s +rhoEqn assamble = 0.000171 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 4.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001085 s +UEqn assamble = 0.000588 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000497 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001367 s +YEqn assamble = 0.000501 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000102 s +YEqn correct boundary = 0 s +EEqn Time = 0.000356 s +EEqn assamble = 0.000265 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 3.26 s ClockTime = 4 s +Courant Number mean: 3.56316e-05 max: 0.00377162 +Time = 9e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 21 new parcels + +Cloud: sprayCloud + Current number of parcels = 565 + Current mass in system = 1.02848e-10 + Linear momentum = (3.83639e-13 -1.01102e-09 0) + |Linear momentum| = 1.01102e-09 + Linear kinetic energy = 5.54501e-09 + model1: + number of parcels added = 565 + mass introduced = 1.02963e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.204, 479.379 + Mass transfer phase change = 1.14441e-13 + D10, D32, Dmax (mu) = 38.11, 85.7319, 149.183 + Liquid penetration 95% mass (m) = 0.000433155 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0240313, Final residual = 2.54446e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.032919, Final residual = 6.94233e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0222377, Final residual = 4.40157e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0176144, Final residual = 3.6786e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0140832, Final residual = 3.0356e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0140834, Final residual = 3.04291e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0239114, Final residual = 5.96984e-07, No Iterations 1 +min/max(T) = 747.546, 801.221 +GAMG: Solving for p, Initial residual = 0.0331114, Final residual = 0.000482095, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.37237e-07, global = 1.13764e-07, cumulative = 2.63529e-06 +GAMG: Solving for p, Initial residual = 0.00045236, Final residual = 6.86947e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.10352e-07, global = 1.10312e-07, cumulative = 2.7456e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000468493, Final residual = 2.16717e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0163564, Final residual = 2.06194e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.091509 s +other Time = 0 s +rho Equations = 0.000152 s +U Equations = 0.001145 s +Y Equations = 0.00229582 s +E Equations = 0.000521 s +p Equations = 0.001804 s +calculate parcels = 0.304413 s +chemistry correctThermo = 0.00199 s +turbulence correct = 0.000942 s +combustion correct(in Y) = 0.0824882 s +percentage of chemistry = 90.1422 % +percentage of rho/U/Y/E = 4.49553 % +========Time details of each equation======= +rhoEqn Time = 0.000281 s +rhoEqn assamble = 0.000213 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001142 s +UEqn assamble = 0.000662 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00048 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001661 s +YEqn assamble = 0.000626 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000174 s +YEqn correct boundary = 0 s +EEqn Time = 0.000401 s +EEqn assamble = 0.000286 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 3.37 s ClockTime = 4 s +Courant Number mean: 3.82215e-05 max: 0.00404355 +Time = 9.25e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 28 new parcels + +Cloud: sprayCloud + Current number of parcels = 593 + Current mass in system = 1.07573e-10 + Linear momentum = (4.19461e-12 -1.07085e-09 0) + |Linear momentum| = 1.07086e-09 + Linear kinetic energy = 5.93948e-09 + model1: + number of parcels added = 593 + mass introduced = 1.07697e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.207, 482.325 + Mass transfer phase change = 1.24515e-13 + D10, D32, Dmax (mu) = 38.6967, 86.0042, 148.803 + Liquid penetration 95% mass (m) = 0.000453426 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0228499, Final residual = 2.17405e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0321067, Final residual = 6.7633e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0213768, Final residual = 4.49155e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0170003, Final residual = 3.71798e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0135484, Final residual = 2.98076e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0135486, Final residual = 2.98779e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0230047, Final residual = 5.97687e-07, No Iterations 1 +min/max(T) = 743.479, 801.331 +GAMG: Solving for p, Initial residual = 0.0315825, Final residual = 0.000285632, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.33149e-07, global = 1.18456e-07, cumulative = 2.86406e-06 +GAMG: Solving for p, Initial residual = 0.000267209, Final residual = 3.56057e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.16135e-07, global = 1.16113e-07, cumulative = 2.98017e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.00046337, Final residual = 2.15105e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0159213, Final residual = 2.00892e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.0802 s +other Time = 0 s +rho Equations = 0.000241 s +U Equations = 0.00172 s +Y Equations = 0.00247482 s +E Equations = 0.000514 s +p Equations = 0.001835 s +calculate parcels = 0.319734 s +chemistry correctThermo = 0.001982 s +turbulence correct = 0.000995 s +combustion correct(in Y) = 0.0701962 s +percentage of chemistry = 87.5264 % +percentage of rho/U/Y/E = 6.17185 % +========Time details of each equation======= +rhoEqn Time = 0.000365 s +rhoEqn assamble = 0.000281 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001719 s +UEqn assamble = 0.000962 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000757 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001349 s +YEqn assamble = 0.000556 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -8.3e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000385 s +EEqn assamble = 0.000287 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 3.45 s ClockTime = 4 s +Courant Number mean: 4.08923e-05 max: 0.00429819 +Time = 9.5e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 42 new parcels + +Cloud: sprayCloud + Current number of parcels = 635 + Current mass in system = 1.14549e-10 + Linear momentum = (5.5428e-12 -1.16151e-09 0) + |Linear momentum| = 1.16152e-09 + Linear kinetic energy = 6.54821e-09 + model1: + number of parcels added = 635 + mass introduced = 1.14684e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.225, 485.076 + Mass transfer phase change = 1.35492e-13 + D10, D32, Dmax (mu) = 37.9478, 85.0524, 148.771 + Liquid penetration 95% mass (m) = 0.000473379 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0215574, Final residual = 1.93975e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0314899, Final residual = 6.6037e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.021436, Final residual = 4.80979e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0168655, Final residual = 3.88674e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0131586, Final residual = 2.95933e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0131588, Final residual = 2.96614e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0231566, Final residual = 6.24441e-07, No Iterations 1 +min/max(T) = 739.022, 801.446 +GAMG: Solving for p, Initial residual = 0.0325517, Final residual = 0.00103246, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.92599e-07, global = 1.46942e-07, cumulative = 3.12711e-06 +GAMG: Solving for p, Initial residual = 0.000977196, Final residual = 3.78988e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.26547e-07, global = 1.26521e-07, cumulative = 3.25363e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000458431, Final residual = 2.13585e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0155161, Final residual = 1.95922e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.068419 s +other Time = 1e-06 s +rho Equations = 0.000155 s +U Equations = 0.001269 s +Y Equations = 0.0021594 s +E Equations = 0.000491 s +p Equations = 0.001963 s +calculate parcels = 0.334071 s +chemistry correctThermo = 0.001961 s +turbulence correct = 0.000895 s +combustion correct(in Y) = 0.0593486 s +percentage of chemistry = 86.7429 % +percentage of rho/U/Y/E = 5.95507 % +========Time details of each equation======= +rhoEqn Time = 0.000277 s +rhoEqn assamble = 0.000217 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001268 s +UEqn assamble = 0.0008 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000468 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001533 s +YEqn assamble = 0.000534 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.3e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000369 s +EEqn assamble = 0.000278 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 3.55 s ClockTime = 4 s +Courant Number mean: 4.39143e-05 max: 0.00468186 +Time = 9.75e-05 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 35 new parcels + +Cloud: sprayCloud + Current number of parcels = 670 + Current mass in system = 1.20328e-10 + Linear momentum = (4.75514e-12 -1.23511e-09 0) + |Linear momentum| = 1.23512e-09 + Linear kinetic energy = 7.03353e-09 + model1: + number of parcels added = 670 + mass introduced = 1.20475e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.202, 487.638 + Mass transfer phase change = 1.47081e-13 + D10, D32, Dmax (mu) = 37.69, 84.6965, 148.967 + Liquid penetration 95% mass (m) = 0.000493852 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0251647, Final residual = 2.04379e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0314917, Final residual = 6.57246e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0206669, Final residual = 4.86974e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0163077, Final residual = 3.91716e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0126576, Final residual = 2.90605e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0126578, Final residual = 2.91223e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.022479, Final residual = 6.27604e-07, No Iterations 1 +min/max(T) = 734.46, 801.556 +GAMG: Solving for p, Initial residual = 0.0324128, Final residual = 0.000534271, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.68805e-07, global = 1.41888e-07, cumulative = 3.39552e-06 +GAMG: Solving for p, Initial residual = 0.000504818, Final residual = 7.00741e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.33629e-07, global = 1.33581e-07, cumulative = 3.5291e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000453717, Final residual = 2.12193e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0151317, Final residual = 1.91264e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.064962 s +other Time = 0 s +rho Equations = 0.000143 s +U Equations = 0.00105 s +Y Equations = 0.00205992 s +E Equations = 0.000498 s +p Equations = 0.001832 s +calculate parcels = 0.348736 s +chemistry correctThermo = 0.001985 s +turbulence correct = 0.000936 s +combustion correct(in Y) = 0.0562811 s +percentage of chemistry = 86.6369 % +percentage of rho/U/Y/E = 5.77403 % +========Time details of each equation======= +rhoEqn Time = 0.000262 s +rhoEqn assamble = 0.000208 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001049 s +UEqn assamble = 0.000639 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00041 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001505 s +YEqn assamble = 0.000541 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000149 s +YEqn correct boundary = 0 s +EEqn Time = 0.000371 s +EEqn assamble = 0.000276 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 3.63 s ClockTime = 4 s +Courant Number mean: 4.71679e-05 max: 0.00499062 +Time = 0.0001 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 11 new parcels + +Cloud: sprayCloud + Current number of parcels = 681 + Current mass in system = 1.22117e-10 + Linear momentum = (5.35485e-12 -1.25271e-09 0) + |Linear momentum| = 1.25272e-09 + Linear kinetic energy = 7.12327e-09 + model1: + number of parcels added = 681 + mass introduced = 1.22276e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.244, 490.022 + Mass transfer phase change = 1.59041e-13 + D10, D32, Dmax (mu) = 37.93, 84.4747, 148.644 + Liquid penetration 95% mass (m) = 0.000514582 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.02666, Final residual = 2.4591e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0310075, Final residual = 6.54596e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0195456, Final residual = 5.03306e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0156506, Final residual = 4.02333e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.012292, Final residual = 2.94501e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0122922, Final residual = 2.95113e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.021113, Final residual = 6.3537e-07, No Iterations 1 +min/max(T) = 730.241, 801.674 +GAMG: Solving for p, Initial residual = 0.0350369, Final residual = 0.00146673, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.42296e-07, global = 1.67857e-07, cumulative = 3.69696e-06 +GAMG: Solving for p, Initial residual = 0.00140202, Final residual = 4.45456e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.37883e-07, global = 1.3785e-07, cumulative = 3.83481e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000449187, Final residual = 2.10881e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0147603, Final residual = 1.86818e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.06688 s +other Time = 0 s +rho Equations = 0.000142 s +U Equations = 0.001047 s +Y Equations = 0.00207211 s +E Equations = 0.000742 s +p Equations = 0.001942 s +calculate parcels = 0.363791 s +chemistry correctThermo = 0.001899 s +turbulence correct = 0.000893 s +combustion correct(in Y) = 0.0579919 s +percentage of chemistry = 86.7104 % +percentage of rho/U/Y/E = 5.98551 % +========Time details of each equation======= +rhoEqn Time = 0.000259 s +rhoEqn assamble = 0.000208 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001046 s +UEqn assamble = 0.000633 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000413 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001486 s +YEqn assamble = 0.000537 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00014 s +YEqn correct boundary = 0 s +EEqn Time = 0.000576 s +EEqn assamble = 0.000467 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000109 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 3.75 s ClockTime = 4 s +Courant Number mean: 5.02463e-05 max: 0.00512728 +Time = 0.0001025 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 29 new parcels + +Cloud: sprayCloud + Current number of parcels = 710 + Current mass in system = 1.26719e-10 + Linear momentum = (4.85014e-12 -1.30952e-09 0) + |Linear momentum| = 1.30953e-09 + Linear kinetic energy = 7.48961e-09 + model1: + number of parcels added = 710 + mass introduced = 1.2689e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.197, 492.225 + Mass transfer phase change = 1.71604e-13 + D10, D32, Dmax (mu) = 38.3521, 84.6935, 149.141 + Liquid penetration 95% mass (m) = 0.000535192 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.021445, Final residual = 2.75526e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.029773, Final residual = 6.44779e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.019067, Final residual = 5.53932e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0155128, Final residual = 4.36111e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0123639, Final residual = 3.11814e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0123641, Final residual = 3.12451e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0205326, Final residual = 6.77385e-07, No Iterations 1 +min/max(T) = 726.331, 801.808 +GAMG: Solving for p, Initial residual = 0.0341594, Final residual = 0.00136257, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.49113e-07, global = 1.81434e-07, cumulative = 4.01624e-06 +GAMG: Solving for p, Initial residual = 0.00130354, Final residual = 2.05712e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.44814e-07, global = 1.44797e-07, cumulative = 4.16104e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000444765, Final residual = 2.09573e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0144048, Final residual = 1.82531e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.080767 s +other Time = 0 s +rho Equations = 0.000165 s +U Equations = 0.001254 s +Y Equations = 0.00210993 s +E Equations = 0.0005 s +p Equations = 0.002448 s +calculate parcels = 0.38559 s +chemistry correctThermo = 0.002013 s +turbulence correct = 0.001016 s +combustion correct(in Y) = 0.0710801 s +percentage of chemistry = 88.0063 % +percentage of rho/U/Y/E = 4.98834 % +========Time details of each equation======= +rhoEqn Time = 0.000371 s +rhoEqn assamble = 0.000242 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000129 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001252 s +UEqn assamble = 0.000715 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000537 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001339 s +YEqn assamble = 0.000536 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 3.4e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000377 s +EEqn assamble = 0.000282 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 3.85 s ClockTime = 4 s +Courant Number mean: 5.31288e-05 max: 0.00526856 +Time = 0.000105 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 24 new parcels + +Cloud: sprayCloud + Current number of parcels = 734 + Current mass in system = 1.30469e-10 + Linear momentum = (6.40529e-12 -1.35419e-09 0) + |Linear momentum| = 1.3542e-09 + Linear kinetic energy = 7.76917e-09 + model1: + number of parcels added = 734 + mass introduced = 1.30654e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.227, 494.25 + Mass transfer phase change = 1.84733e-13 + D10, D32, Dmax (mu) = 38.7829, 84.5526, 148.872 + Liquid penetration 95% mass (m) = 0.00055642 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.018048, Final residual = 2.94953e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0287851, Final residual = 6.36795e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0185374, Final residual = 5.91157e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.015579, Final residual = 4.67808e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0128924, Final residual = 3.39626e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0128926, Final residual = 3.40315e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0200822, Final residual = 7.05569e-07, No Iterations 1 +min/max(T) = 722.766, 801.944 +GAMG: Solving for p, Initial residual = 0.0322456, Final residual = 0.000888477, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.22269e-07, global = 1.70884e-07, cumulative = 4.33192e-06 +GAMG: Solving for p, Initial residual = 0.000847213, Final residual = 7.59456e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.51386e-07, global = 1.51322e-07, cumulative = 4.48324e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000440429, Final residual = 2.08262e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.014063, Final residual = 1.78385e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.086612 s +other Time = 0 s +rho Equations = 0.000102 s +U Equations = 0.000911 s +Y Equations = 0.00225327 s +E Equations = 0.000595 s +p Equations = 0.001736 s +calculate parcels = 0.403566 s +chemistry correctThermo = 0.002331 s +turbulence correct = 0.00087 s +combustion correct(in Y) = 0.0776727 s +percentage of chemistry = 89.6789 % +percentage of rho/U/Y/E = 4.45812 % +========Time details of each equation======= +rhoEqn Time = 0.000213 s +rhoEqn assamble = 0.000166 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 4.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000911 s +UEqn assamble = 0.000504 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000407 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001743 s +YEqn assamble = 0.000626 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000216 s +YEqn correct boundary = 0 s +EEqn Time = 0.000443 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 3.96 s ClockTime = 4 s +Courant Number mean: 5.58715e-05 max: 0.00539721 +Time = 0.0001075 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 34 new parcels + +Cloud: sprayCloud + Current number of parcels = 768 + Current mass in system = 1.35693e-10 + Linear momentum = (5.6917e-12 -1.41936e-09 0) + |Linear momentum| = 1.41937e-09 + Linear kinetic energy = 8.19329e-09 + model1: + number of parcels added = 768 + mass introduced = 1.35892e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.187, 496.109 + Mass transfer phase change = 1.98444e-13 + D10, D32, Dmax (mu) = 39.2545, 84.9516, 148.617 + Liquid penetration 95% mass (m) = 0.000576322 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0160716, Final residual = 2.91055e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0280388, Final residual = 6.21619e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.018052, Final residual = 6.15171e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0157434, Final residual = 5.03894e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0135993, Final residual = 3.65483e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0135995, Final residual = 3.66223e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0196258, Final residual = 7.19411e-07, No Iterations 1 +min/max(T) = 719.526, 802.08 +GAMG: Solving for p, Initial residual = 0.0304456, Final residual = 0.000623743, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.10183e-07, global = 1.67566e-07, cumulative = 4.65081e-06 +GAMG: Solving for p, Initial residual = 0.000591751, Final residual = 6.37942e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.58092e-07, global = 1.58036e-07, cumulative = 4.80885e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000436207, Final residual = 2.06958e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0137352, Final residual = 1.74399e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.090298 s +other Time = 0 s +rho Equations = 0.000109 s +U Equations = 0.000925 s +Y Equations = 0.00232618 s +E Equations = 0.000604 s +p Equations = 0.002164 s +calculate parcels = 0.424968 s +chemistry correctThermo = 0.002764 s +turbulence correct = 0.001102 s +combustion correct(in Y) = 0.0801598 s +percentage of chemistry = 88.7725 % +percentage of rho/U/Y/E = 4.39011 % +========Time details of each equation======= +rhoEqn Time = 0.000248 s +rhoEqn assamble = 0.000197 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000925 s +UEqn assamble = 0.000522 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000403 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001787 s +YEqn assamble = 0.000628 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000243 s +YEqn correct boundary = 0 s +EEqn Time = 0.000449 s +EEqn assamble = 0.000326 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000123 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 4.07 s ClockTime = 4 s +Courant Number mean: 5.8531e-05 max: 0.00553379 +Time = 0.00011 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 27 new parcels + +Cloud: sprayCloud + Current number of parcels = 795 + Current mass in system = 1.39794e-10 + Linear momentum = (6.37331e-12 -1.46861e-09 0) + |Linear momentum| = 1.46862e-09 + Linear kinetic energy = 8.50356e-09 + model1: + number of parcels added = 795 + mass introduced = 1.40007e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.178, 497.813 + Mass transfer phase change = 2.12725e-13 + D10, D32, Dmax (mu) = 39.6036, 85.0904, 148.417 + Liquid penetration 95% mass (m) = 0.000596675 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0137593, Final residual = 2.49234e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0271986, Final residual = 6.02822e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0175831, Final residual = 6.25685e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0156875, Final residual = 5.22439e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0138959, Final residual = 3.73163e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0138961, Final residual = 3.73921e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0191107, Final residual = 7.1932e-07, No Iterations 1 +min/max(T) = 716.604, 802.217 +GAMG: Solving for p, Initial residual = 0.0286717, Final residual = 0.000538355, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.11493e-07, global = 1.72143e-07, cumulative = 4.98099e-06 +GAMG: Solving for p, Initial residual = 0.000509421, Final residual = 5.4818e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.64652e-07, global = 1.64603e-07, cumulative = 5.14559e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000432099, Final residual = 2.05677e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0134222, Final residual = 1.7059e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.084126 s +other Time = 0 s +rho Equations = 0.000175 s +U Equations = 0.001205 s +Y Equations = 0.0023301 s +E Equations = 0.000604 s +p Equations = 0.002216 s +calculate parcels = 0.44638 s +chemistry correctThermo = 0.002792 s +turbulence correct = 0.001049 s +combustion correct(in Y) = 0.0734929 s +percentage of chemistry = 87.3605 % +percentage of rho/U/Y/E = 5.12814 % +========Time details of each equation======= +rhoEqn Time = 0.000315 s +rhoEqn assamble = 0.000249 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001204 s +UEqn assamble = 0.000701 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000503 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001676 s +YEqn assamble = 0.000624 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000166 s +YEqn correct boundary = 0 s +EEqn Time = 0.000445 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 4.17 s ClockTime = 5 s +Courant Number mean: 6.11478e-05 max: 0.0056788 +Time = 0.0001125 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 36 new parcels + +Cloud: sprayCloud + Current number of parcels = 831 + Current mass in system = 1.45184e-10 + Linear momentum = (8.09454e-12 -1.53566e-09 0) + |Linear momentum| = 1.53568e-09 + Linear kinetic energy = 8.93844e-09 + model1: + number of parcels added = 831 + mass introduced = 1.45411e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.186, 499.376 + Mass transfer phase change = 2.27713e-13 + D10, D32, Dmax (mu) = 39.9456, 84.9672, 148.42 + Liquid penetration 95% mass (m) = 0.000618825 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0114837, Final residual = 1.912e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0266257, Final residual = 5.86196e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0173053, Final residual = 6.35152e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0156758, Final residual = 5.35829e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0141165, Final residual = 3.74217e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0141166, Final residual = 3.74978e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0188503, Final residual = 7.1976e-07, No Iterations 1 +min/max(T) = 713.865, 802.356 +GAMG: Solving for p, Initial residual = 0.0274784, Final residual = 0.000624823, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.28593e-07, global = 1.86988e-07, cumulative = 5.33258e-06 +GAMG: Solving for p, Initial residual = 0.000590968, Final residual = 9.63309e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.72843e-07, global = 1.72752e-07, cumulative = 5.50533e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000428094, Final residual = 2.04431e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0131259, Final residual = 1.66971e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.080246 s +other Time = 1e-06 s +rho Equations = 9.8e-05 s +U Equations = 0.000982 s +Y Equations = 0.00223365 s +E Equations = 0.000604 s +p Equations = 0.002251 s +calculate parcels = 0.467215 s +chemistry correctThermo = 0.002744 s +turbulence correct = 0.001043 s +combustion correct(in Y) = 0.0701504 s +percentage of chemistry = 87.4191 % +percentage of rho/U/Y/E = 4.88205 % +========Time details of each equation======= +rhoEqn Time = 0.000257 s +rhoEqn assamble = 0.000201 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000982 s +UEqn assamble = 0.000585 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000397 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001706 s +YEqn assamble = 0.000609 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000228 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000327 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000123 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 4.28 s ClockTime = 5 s +Courant Number mean: 6.38643e-05 max: 0.0058899 +Time = 0.000115 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 28 new parcels + +Cloud: sprayCloud + Current number of parcels = 859 + Current mass in system = 1.49334e-10 + Linear momentum = (8.39555e-12 -1.58511e-09 0) + |Linear momentum| = 1.58513e-09 + Linear kinetic energy = 9.24662e-09 + model1: + number of parcels added = 859 + mass introduced = 1.49577e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.179, 500.813 + Mass transfer phase change = 2.43414e-13 + D10, D32, Dmax (mu) = 39.7245, 84.3903, 148.423 + Liquid penetration 95% mass (m) = 0.000638689 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.011798, Final residual = 1.46521e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0262647, Final residual = 5.74787e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0169764, Final residual = 6.35409e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0155581, Final residual = 5.40283e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0141839, Final residual = 3.69197e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.014184, Final residual = 3.6995e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0185546, Final residual = 7.12778e-07, No Iterations 1 +min/max(T) = 711.351, 802.496 +GAMG: Solving for p, Initial residual = 0.0271922, Final residual = 0.000559131, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.33705e-07, global = 1.91882e-07, cumulative = 5.69721e-06 +GAMG: Solving for p, Initial residual = 0.000531145, Final residual = 7.52018e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.81038e-07, global = 1.80965e-07, cumulative = 5.87818e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000424218, Final residual = 2.03236e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0128425, Final residual = 1.63541e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.089247 s +other Time = 1e-06 s +rho Equations = 0.000138 s +U Equations = 0.001131 s +Y Equations = 0.00249758 s +E Equations = 0.000623 s +p Equations = 0.002199 s +calculate parcels = 0.490556 s +chemistry correctThermo = 0.002764 s +turbulence correct = 0.001108 s +combustion correct(in Y) = 0.0786214 s +percentage of chemistry = 88.0942 % +percentage of rho/U/Y/E = 4.91846 % +========Time details of each equation======= +rhoEqn Time = 0.000274 s +rhoEqn assamble = 0.000216 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00113 s +UEqn assamble = 0.000638 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000492 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001851 s +YEqn assamble = 0.000652 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000273 s +YEqn correct boundary = 0 s +EEqn Time = 0.000461 s +EEqn assamble = 0.000342 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000119 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 4.39 s ClockTime = 5 s +Courant Number mean: 6.6715e-05 max: 0.00610397 +Time = 0.0001175 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 39 new parcels + +Cloud: sprayCloud + Current number of parcels = 898 + Current mass in system = 1.55038e-10 + Linear momentum = (6.19037e-12 -1.65613e-09 0) + |Linear momentum| = 1.65614e-09 + Linear kinetic energy = 9.70673e-09 + model1: + number of parcels added = 898 + mass introduced = 1.55297e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.176, 502.133 + Mass transfer phase change = 2.59863e-13 + D10, D32, Dmax (mu) = 40.1375, 84.2769, 148.426 + Liquid penetration 95% mass (m) = 0.000661107 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0142521, Final residual = 1.54599e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0262245, Final residual = 5.70551e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0166798, Final residual = 6.31928e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0154211, Final residual = 5.39856e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0141885, Final residual = 3.64508e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0141885, Final residual = 3.65229e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0183074, Final residual = 7.04893e-07, No Iterations 1 +min/max(T) = 709.003, 802.64 +GAMG: Solving for p, Initial residual = 0.0268445, Final residual = 0.000501949, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.38801e-07, global = 2.02371e-07, cumulative = 6.08055e-06 +GAMG: Solving for p, Initial residual = 0.0004765, Final residual = 4.03044e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.89635e-07, global = 1.89593e-07, cumulative = 6.27014e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000420483, Final residual = 2.02111e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.012572, Final residual = 1.6026e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.069208 s +other Time = 0 s +rho Equations = 0.000105 s +U Equations = 0.000911 s +Y Equations = 0.0024907 s +E Equations = 0.000529 s +p Equations = 0.001771 s +calculate parcels = 0.511434 s +chemistry correctThermo = 0.001931 s +turbulence correct = 0.000891 s +combustion correct(in Y) = 0.0604433 s +percentage of chemistry = 87.3357 % +percentage of rho/U/Y/E = 5.83126 % +========Time details of each equation======= +rhoEqn Time = 0.000221 s +rhoEqn assamble = 0.000174 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 4.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00091 s +UEqn assamble = 0.000501 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000409 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001887 s +YEqn assamble = 0.000688 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000266 s +YEqn correct boundary = 0 s +EEqn Time = 0.000395 s +EEqn assamble = 0.000292 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000103 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 4.48 s ClockTime = 5 s +Courant Number mean: 6.98261e-05 max: 0.00635098 +Time = 0.00012 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 26 new parcels + +Cloud: sprayCloud + Current number of parcels = 924 + Current mass in system = 1.58809e-10 + Linear momentum = (5.62104e-12 -1.69982e-09 0) + |Linear momentum| = 1.69983e-09 + Linear kinetic energy = 9.97242e-09 + model1: + number of parcels added = 924 + mass introduced = 1.59085e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.158, 503.352 + Mass transfer phase change = 2.76846e-13 + D10, D32, Dmax (mu) = 40.4467, 84.2702, 149.237 + Liquid penetration 95% mass (m) = 0.000683101 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0167979, Final residual = 1.77991e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0261146, Final residual = 5.70392e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0161363, Final residual = 6.14485e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0150694, Final residual = 5.27533e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0140127, Final residual = 3.55552e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0140128, Final residual = 3.56253e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0177037, Final residual = 6.80429e-07, No Iterations 1 +min/max(T) = 707.01, 802.789 +GAMG: Solving for p, Initial residual = 0.0281202, Final residual = 0.000659352, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.64345e-07, global = 2.02578e-07, cumulative = 6.47272e-06 +GAMG: Solving for p, Initial residual = 0.000630234, Final residual = 1.60397e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.95762e-07, global = 1.95745e-07, cumulative = 6.66847e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000416918, Final residual = 2.01103e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0123117, Final residual = 1.57132e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.087919 s +other Time = 0 s +rho Equations = 0.000135 s +U Equations = 0.001091 s +Y Equations = 0.00227377 s +E Equations = 0.000585 s +p Equations = 0.002488 s +calculate parcels = 0.533444 s +chemistry correctThermo = 0.002895 s +turbulence correct = 0.001032 s +combustion correct(in Y) = 0.0771892 s +percentage of chemistry = 87.7958 % +percentage of rho/U/Y/E = 4.64606 % +========Time details of each equation======= +rhoEqn Time = 0.000282 s +rhoEqn assamble = 0.000223 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00109 s +UEqn assamble = 0.000613 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000477 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001663 s +YEqn assamble = 0.000613 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000175 s +YEqn correct boundary = 0 s +EEqn Time = 0.000429 s +EEqn assamble = 0.000319 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00011 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 4.59 s ClockTime = 5 s +Courant Number mean: 7.30325e-05 max: 0.00654271 +Time = 0.0001225 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 25 new parcels + +Cloud: sprayCloud + Current number of parcels = 949 + Current mass in system = 1.62379e-10 + Linear momentum = (6.26536e-12 -1.74061e-09 0) + |Linear momentum| = 1.74063e-09 + Linear kinetic energy = 1.02164e-08 + model1: + number of parcels added = 949 + mass introduced = 1.62673e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.189, 504.474 + Mass transfer phase change = 2.94404e-13 + D10, D32, Dmax (mu) = 40.7204, 84.0701, 149.154 + Liquid penetration 95% mass (m) = 0.000704689 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0171364, Final residual = 2.05166e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0259779, Final residual = 5.68849e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0157084, Final residual = 6.08624e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0147696, Final residual = 5.22742e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.013831, Final residual = 3.48281e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.013831, Final residual = 3.48963e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0171427, Final residual = 6.65713e-07, No Iterations 1 +min/max(T) = 705.133, 802.947 +GAMG: Solving for p, Initial residual = 0.0273357, Final residual = 0.000611825, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.68903e-07, global = 2.13929e-07, cumulative = 6.8824e-06 +GAMG: Solving for p, Initial residual = 0.000584809, Final residual = 1.58197e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.02393e-07, global = 2.02376e-07, cumulative = 7.08477e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000413457, Final residual = 2.00303e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0120659, Final residual = 1.54201e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.08628 s +other Time = 0 s +rho Equations = 0.000148 s +U Equations = 0.001329 s +Y Equations = 0.00194434 s +E Equations = 0.000479 s +p Equations = 0.001871 s +calculate parcels = 0.55857 s +chemistry correctThermo = 0.00198 s +turbulence correct = 0.000917 s +combustion correct(in Y) = 0.0774477 s +percentage of chemistry = 89.7632 % +percentage of rho/U/Y/E = 4.52057 % +========Time details of each equation======= +rhoEqn Time = 0.000261 s +rhoEqn assamble = 0.000206 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001328 s +UEqn assamble = 0.000824 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000504 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.0013 s +YEqn assamble = 0.000511 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 7.1e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000365 s +EEqn assamble = 0.000272 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 4.7 s ClockTime = 5 s +Courant Number mean: 7.65314e-05 max: 0.00681777 +Time = 0.000125 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 37 new parcels + +Cloud: sprayCloud + Current number of parcels = 986 + Current mass in system = 1.67588e-10 + Linear momentum = (6.08902e-12 -1.80436e-09 0) + |Linear momentum| = 1.80437e-09 + Linear kinetic energy = 1.06231e-08 + model1: + number of parcels added = 986 + mass introduced = 1.679e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.172, 505.512 + Mass transfer phase change = 3.12559e-13 + D10, D32, Dmax (mu) = 41.1135, 84.1849, 149.056 + Liquid penetration 95% mass (m) = 0.000727546 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.018619, Final residual = 2.22573e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0254914, Final residual = 5.61793e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0152724, Final residual = 6.18416e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.014439, Final residual = 5.28748e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0136, Final residual = 3.45952e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0136, Final residual = 3.46614e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0165942, Final residual = 6.67156e-07, No Iterations 1 +min/max(T) = 703.289, 803.105 +GAMG: Solving for p, Initial residual = 0.0268095, Final residual = 0.000564502, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.6965e-07, global = 2.21335e-07, cumulative = 7.30611e-06 +GAMG: Solving for p, Initial residual = 0.000541574, Final residual = 6.53469e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.09327e-07, global = 2.0925e-07, cumulative = 7.51536e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000410105, Final residual = 1.99568e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0118319, Final residual = 9.87672e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.067578 s +other Time = 0 s +rho Equations = 0.000109 s +U Equations = 0.000933 s +Y Equations = 0.00206226 s +E Equations = 0.000509 s +p Equations = 0.002309 s +calculate parcels = 0.577733 s +chemistry correctThermo = 0.0022 s +turbulence correct = 0.001156 s +combustion correct(in Y) = 0.0581427 s +percentage of chemistry = 86.038 % +percentage of rho/U/Y/E = 5.3468 % +========Time details of each equation======= +rhoEqn Time = 0.000268 s +rhoEqn assamble = 0.000211 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000933 s +UEqn assamble = 0.000528 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000405 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00152 s +YEqn assamble = 0.000559 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000175 s +YEqn correct boundary = 0 s +EEqn Time = 0.000384 s +EEqn assamble = 0.000284 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.0001 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 4.79 s ClockTime = 5 s +Courant Number mean: 8.01833e-05 max: 0.0071204 +Time = 0.0001275 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 30 new parcels + +Cloud: sprayCloud + Current number of parcels = 1016 + Current mass in system = 1.71771e-10 + Linear momentum = (7.40181e-12 -1.85351e-09 0) + |Linear momentum| = 1.85353e-09 + Linear kinetic energy = 1.09247e-08 + model1: + number of parcels added = 1016 + mass introduced = 1.72102e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.179, 506.476 + Mass transfer phase change = 3.31245e-13 + D10, D32, Dmax (mu) = 41.3765, 84.2796, 148.941 + Liquid penetration 95% mass (m) = 0.000749608 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.018824, Final residual = 2.23188e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0250764, Final residual = 5.52914e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0147682, Final residual = 6.22023e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0140549, Final residual = 5.29931e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0133295, Final residual = 3.40175e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0133295, Final residual = 3.40812e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0159586, Final residual = 6.60502e-07, No Iterations 1 +min/max(T) = 701.579, 803.266 +GAMG: Solving for p, Initial residual = 0.0252109, Final residual = 0.000336837, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.54747e-07, global = 2.21339e-07, cumulative = 7.7367e-06 +GAMG: Solving for p, Initial residual = 0.000322045, Final residual = 5.21037e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.15436e-07, global = 2.15374e-07, cumulative = 7.95207e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000406923, Final residual = 1.9897e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0116108, Final residual = 9.70679e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.083271 s +other Time = 0 s +rho Equations = 0.000123 s +U Equations = 0.001077 s +Y Equations = 0.00228219 s +E Equations = 0.0006 s +p Equations = 0.002222 s +calculate parcels = 0.601538 s +chemistry correctThermo = 0.002778 s +turbulence correct = 0.001008 s +combustion correct(in Y) = 0.0730228 s +percentage of chemistry = 87.693 % +percentage of rho/U/Y/E = 4.9023 % +========Time details of each equation======= +rhoEqn Time = 0.00028 s +rhoEqn assamble = 0.000222 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001076 s +UEqn assamble = 0.000603 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000473 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001669 s +YEqn assamble = 0.000626 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000183 s +YEqn correct boundary = 0 s +EEqn Time = 0.000443 s +EEqn assamble = 0.00033 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 4.89 s ClockTime = 5 s +Courant Number mean: 8.39265e-05 max: 0.00738961 +Time = 0.00013 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 24 new parcels + +Cloud: sprayCloud + Current number of parcels = 1040 + Current mass in system = 1.75068e-10 + Linear momentum = (7.78668e-12 -1.88991e-09 0) + |Linear momentum| = 1.88992e-09 + Linear kinetic energy = 1.11349e-08 + model1: + number of parcels added = 1040 + mass introduced = 1.75418e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.158, 507.371 + Mass transfer phase change = 3.50486e-13 + D10, D32, Dmax (mu) = 41.5327, 84.1529, 148.815 + Liquid penetration 95% mass (m) = 0.000771787 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0172234, Final residual = 2.17796e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0246279, Final residual = 5.43437e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0143384, Final residual = 6.29851e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0137257, Final residual = 5.33922e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0130994, Final residual = 3.35327e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0130994, Final residual = 3.35942e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0153797, Final residual = 6.57549e-07, No Iterations 1 +min/max(T) = 700.005, 803.433 +GAMG: Solving for p, Initial residual = 0.0243388, Final residual = 0.000321748, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.60765e-07, global = 2.29821e-07, cumulative = 8.18189e-06 +GAMG: Solving for p, Initial residual = 0.000307552, Final residual = 2.91771e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.21807e-07, global = 2.2177e-07, cumulative = 8.40366e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000403912, Final residual = 1.98489e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0114025, Final residual = 9.54854e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.078484 s +other Time = 0 s +rho Equations = 0.000138 s +U Equations = 0.001183 s +Y Equations = 0.0023068 s +E Equations = 0.000595 s +p Equations = 0.002121 s +calculate parcels = 0.627619 s +chemistry correctThermo = 0.002756 s +turbulence correct = 0.00103 s +combustion correct(in Y) = 0.0681862 s +percentage of chemistry = 86.8791 % +percentage of rho/U/Y/E = 5.38046 % +========Time details of each equation======= +rhoEqn Time = 0.000278 s +rhoEqn assamble = 0.000219 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001181 s +UEqn assamble = 0.000679 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000502 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001676 s +YEqn assamble = 0.000631 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000182 s +YEqn correct boundary = 0 s +EEqn Time = 0.000443 s +EEqn assamble = 0.000322 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000121 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 5 s ClockTime = 5 s +Courant Number mean: 8.76573e-05 max: 0.00766564 +Time = 0.0001325 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 21 new parcels + +Cloud: sprayCloud + Current number of parcels = 1061 + Current mass in system = 1.779e-10 + Linear momentum = (9.51494e-12 -1.91952e-09 0) + |Linear momentum| = 1.91955e-09 + Linear kinetic energy = 1.12971e-08 + model1: + number of parcels added = 1061 + mass introduced = 1.7827e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.184, 508.203 + Mass transfer phase change = 3.70263e-13 + D10, D32, Dmax (mu) = 41.7566, 83.8981, 148.803 + Liquid penetration 95% mass (m) = 0.000794223 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0151744, Final residual = 2.00166e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0240549, Final residual = 5.32622e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0139195, Final residual = 6.35963e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.013377, Final residual = 5.35274e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0128139, Final residual = 3.27943e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0128139, Final residual = 3.28532e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.014835, Final residual = 6.52695e-07, No Iterations 1 +min/max(T) = 698.658, 803.606 +GAMG: Solving for p, Initial residual = 0.0246431, Final residual = 0.000381378, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.75394e-07, global = 2.38295e-07, cumulative = 8.64196e-06 +GAMG: Solving for p, Initial residual = 0.000367482, Final residual = 3.05654e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.27989e-07, global = 2.27949e-07, cumulative = 8.8699e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000401088, Final residual = 1.98152e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0112064, Final residual = 9.40116e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.076837 s +other Time = 1e-06 s +rho Equations = 0.000141 s +U Equations = 0.001171 s +Y Equations = 0.00203715 s +E Equations = 0.000537 s +p Equations = 0.002248 s +calculate parcels = 0.654095 s +chemistry correctThermo = 0.002028 s +turbulence correct = 0.000864 s +combustion correct(in Y) = 0.0676488 s +percentage of chemistry = 88.042 % +percentage of rho/U/Y/E = 5.05766 % +========Time details of each equation======= +rhoEqn Time = 0.000281 s +rhoEqn assamble = 0.000215 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001169 s +UEqn assamble = 0.000675 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000494 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.0014 s +YEqn assamble = 0.000536 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000108 s +YEqn correct boundary = 0 s +EEqn Time = 0.000392 s +EEqn assamble = 0.000293 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 5.1 s ClockTime = 5 s +Courant Number mean: 9.1285e-05 max: 0.00792271 +Time = 0.000135 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 34 new parcels + +Cloud: sprayCloud + Current number of parcels = 1095 + Current mass in system = 1.8241e-10 + Linear momentum = (1.01998e-11 -1.97266e-09 0) + |Linear momentum| = 1.97269e-09 + Linear kinetic energy = 1.16244e-08 + model1: + number of parcels added = 1095 + mass introduced = 1.82801e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.173, 508.973 + Mass transfer phase change = 3.90672e-13 + D10, D32, Dmax (mu) = 41.8955, 83.6781, 148.774 + Liquid penetration 95% mass (m) = 0.000816747 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0127946, Final residual = 1.71789e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0235168, Final residual = 5.21625e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0136107, Final residual = 6.46705e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0131176, Final residual = 5.39867e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0126032, Final residual = 3.20395e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0126032, Final residual = 3.20959e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0144418, Final residual = 6.54347e-07, No Iterations 1 +min/max(T) = 697.373, 803.782 +GAMG: Solving for p, Initial residual = 0.0237666, Final residual = 0.000383264, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.81454e-07, global = 2.44216e-07, cumulative = 9.11412e-06 +GAMG: Solving for p, Initial residual = 0.0003698, Final residual = 5.07177e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.35297e-07, global = 2.35231e-07, cumulative = 9.34935e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000398368, Final residual = 1.97898e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0110187, Final residual = 9.26218e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097666 s +other Time = 0 s +rho Equations = 0.000132 s +U Equations = 0.00114 s +Y Equations = 0.00247694 s +E Equations = 0.000591 s +p Equations = 0.002196 s +calculate parcels = 0.675008 s +chemistry correctThermo = 0.002774 s +turbulence correct = 0.00097 s +combustion correct(in Y) = 0.0871641 s +percentage of chemistry = 89.2471 % +percentage of rho/U/Y/E = 4.44365 % +========Time details of each equation======= +rhoEqn Time = 0.000272 s +rhoEqn assamble = 0.000215 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00114 s +UEqn assamble = 0.000653 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000487 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001818 s +YEqn assamble = 0.000668 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000199 s +YEqn correct boundary = 0 s +EEqn Time = 0.000439 s +EEqn assamble = 0.000326 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 5.22 s ClockTime = 6 s +Courant Number mean: 9.49102e-05 max: 0.00824027 +Time = 0.0001375 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 30 new parcels + +Cloud: sprayCloud + Current number of parcels = 1125 + Current mass in system = 1.86344e-10 + Linear momentum = (1.12319e-11 -2.01752e-09 0) + |Linear momentum| = 2.01755e-09 + Linear kinetic energy = 1.18923e-08 + model1: + number of parcels added = 1125 + mass introduced = 1.86756e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.166, 509.69 + Mass transfer phase change = 4.11592e-13 + D10, D32, Dmax (mu) = 42.1802, 83.5099, 148.718 + Liquid penetration 95% mass (m) = 0.000839496 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0121547, Final residual = 1.41433e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0230256, Final residual = 5.10612e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0131922, Final residual = 6.53053e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0127772, Final residual = 5.41133e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0123357, Final residual = 3.10445e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0123357, Final residual = 3.10981e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0139123, Final residual = 6.5044e-07, No Iterations 1 +min/max(T) = 696.119, 803.957 +GAMG: Solving for p, Initial residual = 0.0237034, Final residual = 0.000428357, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.93639e-07, global = 2.55086e-07, cumulative = 9.60444e-06 +GAMG: Solving for p, Initial residual = 0.000417787, Final residual = 4.80624e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.41188e-07, global = 2.41125e-07, cumulative = 9.84556e-06 +smoothSolver: Solving for epsilon, Initial residual = 0.000395739, Final residual = 1.97697e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0108387, Final residual = 9.13018e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.081177 s +other Time = 0 s +rho Equations = 0.000121 s +U Equations = 0.001125 s +Y Equations = 0.00225006 s +E Equations = 0.000634 s +p Equations = 0.002142 s +calculate parcels = 0.701979 s +chemistry correctThermo = 0.002742 s +turbulence correct = 0.001058 s +combustion correct(in Y) = 0.0709509 s +percentage of chemistry = 87.4028 % +percentage of rho/U/Y/E = 5.08772 % +========Time details of each equation======= +rhoEqn Time = 0.000259 s +rhoEqn assamble = 0.000204 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001125 s +UEqn assamble = 0.000665 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00046 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001671 s +YEqn assamble = 0.000613 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000198 s +YEqn correct boundary = 0 s +EEqn Time = 0.000481 s +EEqn assamble = 0.000364 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 5.33 s ClockTime = 6 s +Courant Number mean: 9.84818e-05 max: 0.00855583 +Time = 0.00014 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 35 new parcels + +Cloud: sprayCloud + Current number of parcels = 1160 + Current mass in system = 1.90877e-10 + Linear momentum = (1.14165e-11 -2.07058e-09 0) + |Linear momentum| = 2.07061e-09 + Linear kinetic energy = 1.22162e-08 + model1: + number of parcels added = 1160 + mass introduced = 1.9131e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.16, 510.359 + Mass transfer phase change = 4.3322e-13 + D10, D32, Dmax (mu) = 40.9343, 83.15, 148.635 + Liquid penetration 95% mass (m) = 0.000862378 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0132505, Final residual = 1.68245e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0227053, Final residual = 5.01187e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0129257, Final residual = 6.68089e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0125402, Final residual = 5.48333e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0121282, Final residual = 3.02239e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0121283, Final residual = 3.0275e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0135594, Final residual = 6.57638e-07, No Iterations 1 +min/max(T) = 694.783, 804.134 +GAMG: Solving for p, Initial residual = 0.0231041, Final residual = 0.000408713, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00216e-07, global = 2.66975e-07, cumulative = 1.01125e-05 +GAMG: Solving for p, Initial residual = 0.000398535, Final residual = 3.56568e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.49335e-07, global = 2.49287e-07, cumulative = 1.03618e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000393201, Final residual = 1.97551e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0106664, Final residual = 9.0059e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.080775 s +other Time = 1e-06 s +rho Equations = 0.000146 s +U Equations = 0.001217 s +Y Equations = 0.00243825 s +E Equations = 0.000622 s +p Equations = 0.002183 s +calculate parcels = 0.732124 s +chemistry correctThermo = 0.002728 s +turbulence correct = 0.000969 s +combustion correct(in Y) = 0.0703007 s +percentage of chemistry = 87.0328 % +percentage of rho/U/Y/E = 5.47602 % +========Time details of each equation======= +rhoEqn Time = 0.000287 s +rhoEqn assamble = 0.000226 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001217 s +UEqn assamble = 0.000693 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000524 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001782 s +YEqn assamble = 0.000662 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000175 s +YEqn correct boundary = 0 s +EEqn Time = 0.00046 s +EEqn assamble = 0.000346 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 5.44 s ClockTime = 6 s +Courant Number mean: 0.000102118 max: 0.00891561 +Time = 0.0001425 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 35 new parcels + +Cloud: sprayCloud + Current number of parcels = 1195 + Current mass in system = 1.95364e-10 + Linear momentum = (1.17767e-11 -2.12283e-09 0) + |Linear momentum| = 2.12287e-09 + Linear kinetic energy = 1.25329e-08 + model1: + number of parcels added = 1195 + mass introduced = 1.9582e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.159, 510.989 + Mass transfer phase change = 4.55442e-13 + D10, D32, Dmax (mu) = 41.1524, 82.8507, 149.218 + Liquid penetration 95% mass (m) = 0.000885096 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0156784, Final residual = 1.95442e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0224951, Final residual = 4.94041e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0125668, Final residual = 6.75061e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0122407, Final residual = 5.49647e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0118836, Final residual = 2.93825e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0118836, Final residual = 2.94306e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0131309, Final residual = 6.57549e-07, No Iterations 1 +min/max(T) = 693.539, 804.312 +GAMG: Solving for p, Initial residual = 0.0225063, Final residual = 0.000257148, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.9089e-07, global = 2.60878e-07, cumulative = 1.06227e-05 +GAMG: Solving for p, Initial residual = 0.000249917, Final residual = 2.73021e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.56169e-07, global = 2.56131e-07, cumulative = 1.08788e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000390878, Final residual = 1.97553e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.010505, Final residual = 8.89128e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.079633 s +other Time = 0 s +rho Equations = 0.000148 s +U Equations = 0.001219 s +Y Equations = 0.00217623 s +E Equations = 0.000543 s +p Equations = 0.00214 s +calculate parcels = 0.756913 s +chemistry correctThermo = 0.002004 s +turbulence correct = 0.000893 s +combustion correct(in Y) = 0.0703248 s +percentage of chemistry = 88.3111 % +percentage of rho/U/Y/E = 5.13133 % +========Time details of each equation======= +rhoEqn Time = 0.000286 s +rhoEqn assamble = 0.000227 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001217 s +UEqn assamble = 0.000696 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000521 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001473 s +YEqn assamble = 0.000574 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 7.8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000403 s +EEqn assamble = 0.000303 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.0001 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 5.55 s ClockTime = 6 s +Courant Number mean: 0.00010577 max: 0.00922551 +Time = 0.000145 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 30 new parcels + +Cloud: sprayCloud + Current number of parcels = 1225 + Current mass in system = 1.99169e-10 + Linear momentum = (1.17802e-11 -2.16545e-09 0) + |Linear momentum| = 2.16549e-09 + Linear kinetic energy = 1.27808e-08 + model1: + number of parcels added = 1225 + mass introduced = 1.99647e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.179, 511.58 + Mass transfer phase change = 4.78143e-13 + D10, D32, Dmax (mu) = 41.4184, 82.761, 149.199 + Liquid penetration 95% mass (m) = 0.000909 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0152614, Final residual = 1.99537e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0221741, Final residual = 4.8842e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0121865, Final residual = 6.74114e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0119646, Final residual = 5.45864e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0117139, Final residual = 2.89111e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.011714, Final residual = 2.89579e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0126411, Final residual = 6.50726e-07, No Iterations 1 +min/max(T) = 692.521, 804.497 +GAMG: Solving for p, Initial residual = 0.0228306, Final residual = 0.000467077, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.26556e-07, global = 2.81186e-07, cumulative = 1.116e-05 +GAMG: Solving for p, Initial residual = 0.000457574, Final residual = 6.29672e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.61735e-07, global = 2.61645e-07, cumulative = 1.14217e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000388809, Final residual = 1.9776e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0103549, Final residual = 8.78712e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.096229 s +other Time = 1e-06 s +rho Equations = 0.000181 s +U Equations = 0.001358 s +Y Equations = 0.00236432 s +E Equations = 0.000591 s +p Equations = 0.002156 s +calculate parcels = 0.784305 s +chemistry correctThermo = 0.002794 s +turbulence correct = 0.001017 s +combustion correct(in Y) = 0.0855797 s +percentage of chemistry = 88.9334 % +percentage of rho/U/Y/E = 4.67044 % +========Time details of each equation======= +rhoEqn Time = 0.00032 s +rhoEqn assamble = 0.000249 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001357 s +UEqn assamble = 0.000798 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000559 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001648 s +YEqn assamble = 0.00062 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000141 s +YEqn correct boundary = 0 s +EEqn Time = 0.000438 s +EEqn assamble = 0.000325 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 5.67 s ClockTime = 6 s +Courant Number mean: 0.000109371 max: 0.00948138 +Time = 0.0001475 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 27 new parcels + +Cloud: sprayCloud + Current number of parcels = 1252 + Current mass in system = 2.02547e-10 + Linear momentum = (1.06338e-11 -2.20208e-09 0) + |Linear momentum| = 2.20211e-09 + Linear kinetic energy = 1.29855e-08 + model1: + number of parcels added = 1252 + mass introduced = 2.03048e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.145, 512.129 + Mass transfer phase change = 5.0134e-13 + D10, D32, Dmax (mu) = 41.6099, 82.5903, 149.189 + Liquid penetration 95% mass (m) = 0.000933448 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0132233, Final residual = 1.93245e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0217032, Final residual = 4.83612e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0118584, Final residual = 6.78548e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0117084, Final residual = 5.45509e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0115276, Final residual = 2.83216e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0115276, Final residual = 2.8367e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0122033, Final residual = 6.45728e-07, No Iterations 1 +min/max(T) = 691.58, 804.689 +GAMG: Solving for p, Initial residual = 0.0223887, Final residual = 0.000306648, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.09343e-07, global = 2.73881e-07, cumulative = 1.16955e-05 +GAMG: Solving for p, Initial residual = 0.000298062, Final residual = 4.57547e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.6744e-07, global = 2.67374e-07, cumulative = 1.19629e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000386851, Final residual = 1.98052e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0102126, Final residual = 8.6893e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.069399 s +other Time = 0 s +rho Equations = 0.000131 s +U Equations = 0.000969 s +Y Equations = 0.00188145 s +E Equations = 0.000489 s +p Equations = 0.00173 s +calculate parcels = 0.812973 s +chemistry correctThermo = 0.001998 s +turbulence correct = 0.000824 s +combustion correct(in Y) = 0.0612195 s +percentage of chemistry = 88.2139 % +percentage of rho/U/Y/E = 5.00073 % +========Time details of each equation======= +rhoEqn Time = 0.000245 s +rhoEqn assamble = 0.000195 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000968 s +UEqn assamble = 0.000561 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000407 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001338 s +YEqn assamble = 0.000493 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000132 s +YEqn correct boundary = 0 s +EEqn Time = 0.000369 s +EEqn assamble = 0.000275 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 5.77 s ClockTime = 6 s +Courant Number mean: 0.00011295 max: 0.00978406 +Time = 0.00015 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 47 new parcels + +Cloud: sprayCloud + Current number of parcels = 1299 + Current mass in system = 2.0836e-10 + Linear momentum = (1.33447e-11 -2.27243e-09 0) + |Linear momentum| = 2.27247e-09 + Linear kinetic energy = 1.34269e-08 + model1: + number of parcels added = 1299 + mass introduced = 2.08885e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.152, 512.639 + Mass transfer phase change = 5.25272e-13 + D10, D32, Dmax (mu) = 41.2764, 82.223, 149.178 + Liquid penetration 95% mass (m) = 0.000957326 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0126623, Final residual = 2.01234e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0213294, Final residual = 4.7852e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0116639, Final residual = 6.92863e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0115446, Final residual = 5.51746e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0113976, Final residual = 2.79585e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0113976, Final residual = 2.80002e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0119836, Final residual = 6.54826e-07, No Iterations 1 +min/max(T) = 690.503, 804.879 +GAMG: Solving for p, Initial residual = 0.0225172, Final residual = 0.000516106, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.44048e-07, global = 3.00764e-07, cumulative = 1.22637e-05 +GAMG: Solving for p, Initial residual = 0.000507104, Final residual = 8.41062e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.75954e-07, global = 2.75833e-07, cumulative = 1.25395e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000384923, Final residual = 1.98369e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0100729, Final residual = 8.59592e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.068295 s +other Time = 1e-06 s +rho Equations = 0.000195 s +U Equations = 0.00135 s +Y Equations = 0.00225288 s +E Equations = 0.000506 s +p Equations = 0.001965 s +calculate parcels = 0.844157 s +chemistry correctThermo = 0.001987 s +turbulence correct = 0.000893 s +combustion correct(in Y) = 0.0589441 s +percentage of chemistry = 86.3081 % +percentage of rho/U/Y/E = 6.3019 % +========Time details of each equation======= +rhoEqn Time = 0.000342 s +rhoEqn assamble = 0.000255 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001349 s +UEqn assamble = 0.000816 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000533 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001575 s +YEqn assamble = 0.000615 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.4e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000377 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 5.87 s ClockTime = 6 s +Courant Number mean: 0.000116727 max: 0.0101722 +Time = 0.0001525 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 33 new parcels + +Cloud: sprayCloud + Current number of parcels = 1332 + Current mass in system = 2.12422e-10 + Linear momentum = (1.27769e-11 -2.31821e-09 0) + |Linear momentum| = 2.31825e-09 + Linear kinetic energy = 1.36945e-08 + model1: + number of parcels added = 1332 + mass introduced = 2.12972e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.147, 513.12 + Mass transfer phase change = 5.49628e-13 + D10, D32, Dmax (mu) = 41.5466, 82.173, 149.133 + Liquid penetration 95% mass (m) = 0.00098129 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0153623, Final residual = 2.0427e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0211319, Final residual = 4.7177e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0112696, Final residual = 6.92137e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0112374, Final residual = 5.47256e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0111761, Final residual = 2.73937e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0111761, Final residual = 2.74339e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0115278, Final residual = 6.46491e-07, No Iterations 1 +min/max(T) = 689.665, 805.064 +GAMG: Solving for p, Initial residual = 0.0224149, Final residual = 0.000349342, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.29713e-07, global = 2.86247e-07, cumulative = 1.28258e-05 +GAMG: Solving for p, Initial residual = 0.000345447, Final residual = 5.83324e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.80812e-07, global = 2.80728e-07, cumulative = 1.31065e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000383311, Final residual = 1.98916e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0099451, Final residual = 8.51287e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.073168 s +other Time = 0 s +rho Equations = 0.000153 s +U Equations = 0.001081 s +Y Equations = 0.00209206 s +E Equations = 0.000504 s +p Equations = 0.001978 s +calculate parcels = 0.868336 s +chemistry correctThermo = 0.002015 s +turbulence correct = 0.000907 s +combustion correct(in Y) = 0.0642239 s +percentage of chemistry = 87.776 % +percentage of rho/U/Y/E = 5.23461 % +========Time details of each equation======= +rhoEqn Time = 0.000278 s +rhoEqn assamble = 0.000222 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001079 s +UEqn assamble = 0.000646 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000433 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00149 s +YEqn assamble = 0.000533 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000126 s +YEqn correct boundary = 0 s +EEqn Time = 0.000379 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 5.96 s ClockTime = 6 s +Courant Number mean: 0.000120428 max: 0.0104224 +Time = 0.000155 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 38 new parcels + +Cloud: sprayCloud + Current number of parcels = 1370 + Current mass in system = 2.17053e-10 + Linear momentum = (1.20596e-11 -2.37197e-09 0) + |Linear momentum| = 2.372e-09 + Linear kinetic energy = 1.40171e-08 + model1: + number of parcels added = 1370 + mass introduced = 2.17628e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.137, 513.569 + Mass transfer phase change = 5.74376e-13 + D10, D32, Dmax (mu) = 41.8201, 82.3285, 149.057 + Liquid penetration 95% mass (m) = 0.00100641 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0131288, Final residual = 1.81318e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0208891, Final residual = 4.67294e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0109372, Final residual = 6.92015e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0109833, Final residual = 5.42083e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0110042, Final residual = 2.71939e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0110042, Final residual = 2.72386e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0111155, Final residual = 6.41102e-07, No Iterations 1 +min/max(T) = 689.028, 805.261 +GAMG: Solving for p, Initial residual = 0.0215201, Final residual = 0.000325825, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.33597e-07, global = 3.00813e-07, cumulative = 1.34073e-05 +GAMG: Solving for p, Initial residual = 0.000319593, Final residual = 4.96408e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.85319e-07, global = 2.85244e-07, cumulative = 1.36925e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000381939, Final residual = 1.9966e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00982647, Final residual = 8.43834e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.066837 s +other Time = 0 s +rho Equations = 0.000147 s +U Equations = 0.001413 s +Y Equations = 0.00207458 s +E Equations = 0.000506 s +p Equations = 0.002007 s +calculate parcels = 0.892899 s +chemistry correctThermo = 0.001932 s +turbulence correct = 0.000881 s +combustion correct(in Y) = 0.0577084 s +percentage of chemistry = 86.342 % +percentage of rho/U/Y/E = 6.19504 % +========Time details of each equation======= +rhoEqn Time = 0.00028 s +rhoEqn assamble = 0.000221 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001412 s +UEqn assamble = 0.000947 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000465 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001449 s +YEqn assamble = 0.000548 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000103 s +YEqn correct boundary = 0 s +EEqn Time = 0.00038 s +EEqn assamble = 0.000276 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000104 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 6.06 s ClockTime = 6 s +Courant Number mean: 0.000124047 max: 0.0106751 +Time = 0.0001575 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 39 new parcels + +Cloud: sprayCloud + Current number of parcels = 1409 + Current mass in system = 2.2177e-10 + Linear momentum = (1.24694e-11 -2.42682e-09 0) + |Linear momentum| = 2.42685e-09 + Linear kinetic energy = 1.43467e-08 + model1: + number of parcels added = 1409 + mass introduced = 2.22369e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.14, 513.985 + Mass transfer phase change = 5.9956e-13 + D10, D32, Dmax (mu) = 42.0595, 82.3054, 148.953 + Liquid penetration 95% mass (m) = 0.00103104 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0105463, Final residual = 1.58981e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0205423, Final residual = 4.62542e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0106399, Final residual = 6.93422e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0107374, Final residual = 5.3926e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.010808, Final residual = 2.68339e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.010808, Final residual = 2.68775e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0107536, Final residual = 6.34996e-07, No Iterations 1 +min/max(T) = 688.423, 805.462 +GAMG: Solving for p, Initial residual = 0.0215012, Final residual = 0.000284533, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.29444e-07, global = 2.9669e-07, cumulative = 1.39892e-05 +GAMG: Solving for p, Initial residual = 0.000281162, Final residual = 3.034e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.90319e-07, global = 2.90273e-07, cumulative = 1.42795e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000380626, Final residual = 2.00494e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00971187, Final residual = 8.37019e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.066912 s +other Time = 0 s +rho Equations = 0.000155 s +U Equations = 0.001088 s +Y Equations = 0.0021473 s +E Equations = 0.000486 s +p Equations = 0.001817 s +calculate parcels = 0.917895 s +chemistry correctThermo = 0.001931 s +turbulence correct = 0.001037 s +combustion correct(in Y) = 0.0580687 s +percentage of chemistry = 86.7837 % +percentage of rho/U/Y/E = 5.79313 % +========Time details of each equation======= +rhoEqn Time = 0.000284 s +rhoEqn assamble = 0.000221 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001086 s +UEqn assamble = 0.000656 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00043 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001568 s +YEqn assamble = 0.000565 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000134 s +YEqn correct boundary = 0 s +EEqn Time = 0.000367 s +EEqn assamble = 0.000275 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 6.15 s ClockTime = 7 s +Courant Number mean: 0.000127698 max: 0.0109901 +Time = 0.00016 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 34 new parcels + +Cloud: sprayCloud + Current number of parcels = 1443 + Current mass in system = 2.25848e-10 + Linear momentum = (1.29376e-11 -2.47257e-09 0) + |Linear momentum| = 2.47261e-09 + Linear kinetic energy = 1.46124e-08 + model1: + number of parcels added = 1443 + mass introduced = 2.26473e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.151, 514.374 + Mass transfer phase change = 6.25174e-13 + D10, D32, Dmax (mu) = 42.2933, 82.0741, 148.82 + Liquid penetration 95% mass (m) = 0.00105612 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.010879, Final residual = 1.62961e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0202319, Final residual = 4.58267e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0103427, Final residual = 6.98223e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0105094, Final residual = 5.38721e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0106515, Final residual = 2.66368e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0106515, Final residual = 2.66795e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0104197, Final residual = 6.31775e-07, No Iterations 1 +min/max(T) = 687.884, 805.659 +GAMG: Solving for p, Initial residual = 0.0209726, Final residual = 0.000219657, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.26246e-07, global = 3.04829e-07, cumulative = 1.45843e-05 +GAMG: Solving for p, Initial residual = 0.000215647, Final residual = 3.18582e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.95277e-07, global = 2.9523e-07, cumulative = 1.48796e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000379466, Final residual = 2.01484e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00960267, Final residual = 8.30809e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094338 s +other Time = 0 s +rho Equations = 0.000178 s +U Equations = 0.001358 s +Y Equations = 0.00246962 s +E Equations = 0.000602 s +p Equations = 0.00224 s +calculate parcels = 0.947586 s +chemistry correctThermo = 0.002761 s +turbulence correct = 0.001059 s +combustion correct(in Y) = 0.0834864 s +percentage of chemistry = 88.4971 % +percentage of rho/U/Y/E = 4.88416 % +========Time details of each equation======= +rhoEqn Time = 0.000321 s +rhoEqn assamble = 0.000251 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001356 s +UEqn assamble = 0.000736 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00062 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001788 s +YEqn assamble = 0.000654 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000162 s +YEqn correct boundary = 0 s +EEqn Time = 0.000442 s +EEqn assamble = 0.00033 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 6.27 s ClockTime = 7 s +Courant Number mean: 0.000131337 max: 0.0112888 +Time = 0.0001625 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 39 new parcels + +Cloud: sprayCloud + Current number of parcels = 1482 + Current mass in system = 2.30483e-10 + Linear momentum = (1.39098e-11 -2.52596e-09 0) + |Linear momentum| = 2.526e-09 + Linear kinetic energy = 1.4931e-08 + model1: + number of parcels added = 1482 + mass introduced = 2.31134e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.164, 514.738 + Mass transfer phase change = 6.51182e-13 + D10, D32, Dmax (mu) = 42.4583, 82.0607, 149.54 + Liquid penetration 95% mass (m) = 0.0010803 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.011925, Final residual = 1.82788e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0200929, Final residual = 4.54965e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0100451, Final residual = 7.01881e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0102762, Final residual = 5.37434e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.010483, Final residual = 2.65842e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.010483, Final residual = 2.6624e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.010107, Final residual = 6.285e-07, No Iterations 1 +min/max(T) = 687.363, 805.858 +GAMG: Solving for p, Initial residual = 0.0210555, Final residual = 0.000232737, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.32913e-07, global = 3.08717e-07, cumulative = 1.51883e-05 +GAMG: Solving for p, Initial residual = 0.000229486, Final residual = 2.63578e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.99797e-07, global = 2.99758e-07, cumulative = 1.5488e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000378441, Final residual = 2.02615e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00949798, Final residual = 8.25146e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.080253 s +other Time = 0 s +rho Equations = 0.000184 s +U Equations = 0.001303 s +Y Equations = 0.0024422 s +E Equations = 0.000609 s +p Equations = 0.002292 s +calculate parcels = 0.983624 s +chemistry correctThermo = 0.002804 s +turbulence correct = 0.001039 s +combustion correct(in Y) = 0.0693768 s +percentage of chemistry = 86.4476 % +percentage of rho/U/Y/E = 5.65486 % +========Time details of each equation======= +rhoEqn Time = 0.000333 s +rhoEqn assamble = 0.000264 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001301 s +UEqn assamble = 0.000783 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000518 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001764 s +YEqn assamble = 0.000644 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000169 s +YEqn correct boundary = 0 s +EEqn Time = 0.000453 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 6.39 s ClockTime = 7 s +Courant Number mean: 0.000135008 max: 0.0115933 +Time = 0.000165 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 55 new parcels + +Cloud: sprayCloud + Current number of parcels = 1537 + Current mass in system = 2.36983e-10 + Linear momentum = (1.34918e-11 -2.6052e-09 0) + |Linear momentum| = 2.60524e-09 + Linear kinetic energy = 1.54287e-08 + model1: + number of parcels added = 1537 + mass introduced = 2.37661e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.161, 515.128 + Mass transfer phase change = 6.77666e-13 + D10, D32, Dmax (mu) = 42.794, 81.968, 149.54 + Liquid penetration 95% mass (m) = 0.00110519 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0136096, Final residual = 2.13647e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0200451, Final residual = 4.53092e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0098051, Final residual = 7.10062e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0100805, Final residual = 5.3803e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0103324, Final residual = 2.6621e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0103325, Final residual = 2.66606e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00989843, Final residual = 6.31917e-07, No Iterations 1 +min/max(T) = 686.776, 806.059 +GAMG: Solving for p, Initial residual = 0.0212041, Final residual = 0.000270262, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.43131e-07, global = 3.1634e-07, cumulative = 1.58044e-05 +GAMG: Solving for p, Initial residual = 0.000266721, Final residual = 4.08173e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.05319e-07, global = 3.05259e-07, cumulative = 1.61096e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000377506, Final residual = 2.03812e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0093966, Final residual = 8.19861e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.076499 s +other Time = 0 s +rho Equations = 0.000143 s +U Equations = 0.001021 s +Y Equations = 0.00231652 s +E Equations = 0.000596 s +p Equations = 0.002158 s +calculate parcels = 1.01608 s +chemistry correctThermo = 0.00278 s +turbulence correct = 0.000997 s +combustion correct(in Y) = 0.0663165 s +percentage of chemistry = 86.6893 % +percentage of rho/U/Y/E = 5.32886 % +========Time details of each equation======= +rhoEqn Time = 0.000287 s +rhoEqn assamble = 0.000225 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00102 s +UEqn assamble = 0.0006 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00042 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001755 s +YEqn assamble = 0.000643 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000219 s +YEqn correct boundary = 0 s +EEqn Time = 0.000439 s +EEqn assamble = 0.000327 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 6.5 s ClockTime = 7 s +Courant Number mean: 0.000138696 max: 0.0119235 +Time = 0.0001675 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 31 new parcels + +Cloud: sprayCloud + Current number of parcels = 1568 + Current mass in system = 2.40641e-10 + Linear momentum = (1.29572e-11 -2.64471e-09 0) + |Linear momentum| = 2.64474e-09 + Linear kinetic energy = 1.56478e-08 + model1: + number of parcels added = 1568 + mass introduced = 2.41346e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.171, 515.477 + Mass transfer phase change = 7.0442e-13 + D10, D32, Dmax (mu) = 43.0224, 81.7999, 149.541 + Liquid penetration 95% mass (m) = 0.00113039 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0149979, Final residual = 2.30255e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.019967, Final residual = 4.50608e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0094786, Final residual = 7.08235e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00984171, Final residual = 5.347e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0101823, Final residual = 2.66009e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0101824, Final residual = 2.664e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00957857, Final residual = 6.24527e-07, No Iterations 1 +min/max(T) = 686.271, 806.259 +GAMG: Solving for p, Initial residual = 0.0212044, Final residual = 0.000241011, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.43446e-07, global = 3.14589e-07, cumulative = 1.64242e-05 +GAMG: Solving for p, Initial residual = 0.000238589, Final residual = 5.2307e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.0844e-07, global = 3.08364e-07, cumulative = 1.67326e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000376808, Final residual = 2.05184e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00930182, Final residual = 8.15157e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.070329 s +other Time = 0 s +rho Equations = 0.000164 s +U Equations = 0.001196 s +Y Equations = 0.00210253 s +E Equations = 0.000482 s +p Equations = 0.002198 s +calculate parcels = 1.04796 s +chemistry correctThermo = 0.002064 s +turbulence correct = 0.001043 s +combustion correct(in Y) = 0.0608885 s +percentage of chemistry = 86.5766 % +percentage of rho/U/Y/E = 5.60869 % +========Time details of each equation======= +rhoEqn Time = 0.000308 s +rhoEqn assamble = 0.000242 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001195 s +UEqn assamble = 0.000704 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000491 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001459 s +YEqn assamble = 0.000541 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.9e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000365 s +EEqn assamble = 0.000272 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 6.6 s ClockTime = 7 s +Courant Number mean: 0.000142267 max: 0.0121903 +Time = 0.00017 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 28 new parcels + +Cloud: sprayCloud + Current number of parcels = 1596 + Current mass in system = 2.43902e-10 + Linear momentum = (1.2328e-11 -2.67859e-09 0) + |Linear momentum| = 2.67862e-09 + Linear kinetic energy = 1.58267e-08 + model1: + number of parcels added = 1596 + mass introduced = 2.44633e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.153, 515.743 + Mass transfer phase change = 7.31453e-13 + D10, D32, Dmax (mu) = 43.1976, 81.6204, 149.543 + Liquid penetration 95% mass (m) = 0.0011568 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0146713, Final residual = 2.40448e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0198903, Final residual = 4.49866e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00919639, Final residual = 7.04152e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00963446, Final residual = 5.27702e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0100506, Final residual = 2.65418e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0100507, Final residual = 2.65808e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00928662, Final residual = 6.15799e-07, No Iterations 1 +min/max(T) = 685.811, 806.464 +GAMG: Solving for p, Initial residual = 0.0212445, Final residual = 0.00022533, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.44807e-07, global = 3.16558e-07, cumulative = 1.70492e-05 +GAMG: Solving for p, Initial residual = 0.000221432, Final residual = 4.87296e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.1166e-07, global = 3.11586e-07, cumulative = 1.73607e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000376292, Final residual = 2.06748e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00921198, Final residual = 8.10995e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.082616 s +other Time = 0 s +rho Equations = 0.000137 s +U Equations = 0.001001 s +Y Equations = 0.00234633 s +E Equations = 0.0006 s +p Equations = 0.002156 s +calculate parcels = 1.07819 s +chemistry correctThermo = 0.002778 s +turbulence correct = 0.001008 s +combustion correct(in Y) = 0.0724237 s +percentage of chemistry = 87.663 % +percentage of rho/U/Y/E = 4.94375 % +========Time details of each equation======= +rhoEqn Time = 0.000275 s +rhoEqn assamble = 0.000216 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001001 s +UEqn assamble = 0.000587 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000414 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001795 s +YEqn assamble = 0.000664 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00023 s +YEqn correct boundary = 0 s +EEqn Time = 0.000443 s +EEqn assamble = 0.000331 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 6.71 s ClockTime = 7 s +Courant Number mean: 0.000145768 max: 0.0124593 +Time = 0.0001725 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 39 new parcels + +Cloud: sprayCloud + Current number of parcels = 1635 + Current mass in system = 2.4839e-10 + Linear momentum = (1.13676e-11 -2.72924e-09 0) + |Linear momentum| = 2.72926e-09 + Linear kinetic energy = 1.61219e-08 + model1: + number of parcels added = 1635 + mass introduced = 2.49149e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.176, 515.941 + Mass transfer phase change = 7.5881e-13 + D10, D32, Dmax (mu) = 43.3413, 81.5249, 149.546 + Liquid penetration 95% mass (m) = 0.00118299 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0147677, Final residual = 2.52184e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0197865, Final residual = 4.50221e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0089557, Final residual = 7.03273e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00945341, Final residual = 5.23168e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00992926, Final residual = 2.65356e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00992929, Final residual = 2.65793e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00906544, Final residual = 6.12283e-07, No Iterations 1 +min/max(T) = 682.155, 806.67 +GAMG: Solving for p, Initial residual = 0.0211937, Final residual = 0.000169307, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.39646e-07, global = 3.20364e-07, cumulative = 1.76811e-05 +GAMG: Solving for p, Initial residual = 0.000164656, Final residual = 2.90099e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.15356e-07, global = 3.15314e-07, cumulative = 1.79964e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000375958, Final residual = 2.08428e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00912631, Final residual = 8.07231e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.07531 s +other Time = 0 s +rho Equations = 0.000133 s +U Equations = 0.000998 s +Y Equations = 0.00199034 s +E Equations = 0.000519 s +p Equations = 0.001879 s +calculate parcels = 1.10626 s +chemistry correctThermo = 0.001987 s +turbulence correct = 0.001073 s +combustion correct(in Y) = 0.0665677 s +percentage of chemistry = 88.3915 % +percentage of rho/U/Y/E = 4.83381 % +========Time details of each equation======= +rhoEqn Time = 0.000271 s +rhoEqn assamble = 0.000199 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000998 s +UEqn assamble = 0.000585 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000413 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00143 s +YEqn assamble = 0.000529 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000133 s +YEqn correct boundary = 0 s +EEqn Time = 0.000399 s +EEqn assamble = 0.000301 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 6.82 s ClockTime = 7 s +Courant Number mean: 0.000149212 max: 0.0127342 +Time = 0.000175 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 43 new parcels + +Cloud: sprayCloud + Current number of parcels = 1678 + Current mass in system = 2.53301e-10 + Linear momentum = (1.24602e-11 -2.78555e-09 0) + |Linear momentum| = 2.78558e-09 + Linear kinetic energy = 1.64547e-08 + model1: + number of parcels added = 1678 + mass introduced = 2.54088e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.152, 516.089 + Mass transfer phase change = 7.86515e-13 + D10, D32, Dmax (mu) = 43.4504, 81.362, 149.525 + Liquid penetration 95% mass (m) = 0.00120841 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0147834, Final residual = 2.51103e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0197507, Final residual = 4.5032e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0087281, Final residual = 6.99711e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00927919, Final residual = 5.17166e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00980582, Final residual = 2.6635e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00980585, Final residual = 2.66787e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00888465, Final residual = 6.07798e-07, No Iterations 1 +min/max(T) = 678.011, 806.875 +GAMG: Solving for p, Initial residual = 0.0213663, Final residual = 0.000178055, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.43246e-07, global = 3.25167e-07, cumulative = 1.83216e-05 +GAMG: Solving for p, Initial residual = 0.000175148, Final residual = 3.84954e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.19379e-07, global = 3.19327e-07, cumulative = 1.86409e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000375804, Final residual = 2.10291e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00904461, Final residual = 8.04004e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.079399 s +other Time = 1e-06 s +rho Equations = 0.000142 s +U Equations = 0.001144 s +Y Equations = 0.00205623 s +E Equations = 0.000483 s +p Equations = 0.001767 s +calculate parcels = 1.14404 s +chemistry correctThermo = 0.001978 s +turbulence correct = 0.000868 s +combustion correct(in Y) = 0.0707498 s +percentage of chemistry = 89.1066 % +percentage of rho/U/Y/E = 4.81774 % +========Time details of each equation======= +rhoEqn Time = 0.000266 s +rhoEqn assamble = 0.000201 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001143 s +UEqn assamble = 0.000665 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000478 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001425 s +YEqn assamble = 0.000524 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000118 s +YEqn correct boundary = 0 s +EEqn Time = 0.000362 s +EEqn assamble = 0.000269 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 6.93 s ClockTime = 7 s +Courant Number mean: 0.000152666 max: 0.0130165 +Time = 0.0001775 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 52 new parcels + +Cloud: sprayCloud + Current number of parcels = 1730 + Current mass in system = 2.59211e-10 + Linear momentum = (1.40633e-11 -2.8554e-09 0) + |Linear momentum| = 2.85543e-09 + Linear kinetic energy = 1.68796e-08 + model1: + number of parcels added = 1730 + mass introduced = 2.60026e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.153, 516.205 + Mass transfer phase change = 8.1458e-13 + D10, D32, Dmax (mu) = 43.6501, 81.3752, 149.472 + Liquid penetration 95% mass (m) = 0.00123449 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0150327, Final residual = 2.45612e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0197962, Final residual = 4.51014e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00851535, Final residual = 6.95066e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00911708, Final residual = 5.10434e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.009692, Final residual = 2.66848e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00969203, Final residual = 2.67282e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00871162, Final residual = 6.0185e-07, No Iterations 1 +min/max(T) = 673.996, 807.079 +GAMG: Solving for p, Initial residual = 0.0216061, Final residual = 0.000184719, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.48328e-07, global = 3.29609e-07, cumulative = 1.89705e-05 +GAMG: Solving for p, Initial residual = 0.000182222, Final residual = 3.27807e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.23514e-07, global = 3.2347e-07, cumulative = 1.9294e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000375871, Final residual = 2.12386e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00896787, Final residual = 8.01372e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.089679 s +other Time = 1e-06 s +rho Equations = 0.000167 s +U Equations = 0.001345 s +Y Equations = 0.00204155 s +E Equations = 0.000501 s +p Equations = 0.001845 s +calculate parcels = 1.18217 s +chemistry correctThermo = 0.002025 s +turbulence correct = 0.000907 s +combustion correct(in Y) = 0.0806605 s +percentage of chemistry = 89.9435 % +percentage of rho/U/Y/E = 4.52118 % +========Time details of each equation======= +rhoEqn Time = 0.000291 s +rhoEqn assamble = 0.000231 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001345 s +UEqn assamble = 0.000825 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00052 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001385 s +YEqn assamble = 0.00052 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000382 s +EEqn assamble = 0.000284 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 7.06 s ClockTime = 7 s +Courant Number mean: 0.000156156 max: 0.0132886 +Time = 0.00018 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 41 new parcels + +Cloud: sprayCloud + Current number of parcels = 1771 + Current mass in system = 2.6386e-10 + Linear momentum = (1.27801e-11 -2.90759e-09 0) + |Linear momentum| = 2.90762e-09 + Linear kinetic energy = 1.71807e-08 + model1: + number of parcels added = 1771 + mass introduced = 2.64703e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.159, 516.304 + Mass transfer phase change = 8.42958e-13 + D10, D32, Dmax (mu) = 43.7974, 81.29, 149.389 + Liquid penetration 95% mass (m) = 0.00126045 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0149278, Final residual = 2.34404e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0198965, Final residual = 4.52858e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00830327, Final residual = 6.87796e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00895773, Final residual = 5.01492e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00958195, Final residual = 2.66843e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00958198, Final residual = 2.67276e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00851593, Final residual = 5.92027e-07, No Iterations 1 +min/max(T) = 670.127, 807.282 +GAMG: Solving for p, Initial residual = 0.0219945, Final residual = 0.000205715, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.55788e-07, global = 3.31503e-07, cumulative = 1.96255e-05 +GAMG: Solving for p, Initial residual = 0.000204281, Final residual = 5.04802e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.27158e-07, global = 3.27086e-07, cumulative = 1.99526e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000376206, Final residual = 2.14743e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00889638, Final residual = 7.99347e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.079542 s +other Time = 0 s +rho Equations = 0.000142 s +U Equations = 0.001144 s +Y Equations = 0.00267599 s +E Equations = 0.000497 s +p Equations = 0.001797 s +calculate parcels = 1.21374 s +chemistry correctThermo = 0.001958 s +turbulence correct = 0.00087 s +combustion correct(in Y) = 0.070264 s +percentage of chemistry = 88.3357 % +percentage of rho/U/Y/E = 5.60583 % +========Time details of each equation======= +rhoEqn Time = 0.000259 s +rhoEqn assamble = 0.000203 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001142 s +UEqn assamble = 0.000632 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00051 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002016 s +YEqn assamble = 0.000674 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000219 s +YEqn correct boundary = 0 s +EEqn Time = 0.000371 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 7.17 s ClockTime = 8 s +Courant Number mean: 0.00015964 max: 0.0135317 +Time = 0.0001825 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 53 new parcels + +Cloud: sprayCloud + Current number of parcels = 1824 + Current mass in system = 2.69835e-10 + Linear momentum = (1.43276e-11 -2.97772e-09 0) + |Linear momentum| = 2.97776e-09 + Linear kinetic energy = 1.76046e-08 + model1: + number of parcels added = 1824 + mass introduced = 2.70707e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.139, 516.397 + Mass transfer phase change = 8.71693e-13 + D10, D32, Dmax (mu) = 44.0725, 81.4191, 149.278 + Liquid penetration 95% mass (m) = 0.00128653 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0144026, Final residual = 2.20769e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0200356, Final residual = 4.56145e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0082339, Final residual = 6.95468e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00881029, Final residual = 5.04004e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00945826, Final residual = 2.66859e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00945828, Final residual = 2.67289e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00835409, Final residual = 5.86115e-07, No Iterations 1 +min/max(T) = 666.378, 807.488 +GAMG: Solving for p, Initial residual = 0.0220161, Final residual = 0.000168032, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.55515e-07, global = 3.35941e-07, cumulative = 2.02885e-05 +GAMG: Solving for p, Initial residual = 0.000167013, Final residual = 2.04667e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.31235e-07, global = 3.31205e-07, cumulative = 2.06197e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000376791, Final residual = 2.17354e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00882931, Final residual = 7.97837e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.082571 s +other Time = 0 s +rho Equations = 0.00013 s +U Equations = 0.001137 s +Y Equations = 0.00238359 s +E Equations = 0.000602 s +p Equations = 0.002226 s +calculate parcels = 1.25484 s +chemistry correctThermo = 0.002795 s +turbulence correct = 0.000988 s +combustion correct(in Y) = 0.0721474 s +percentage of chemistry = 87.3762 % +percentage of rho/U/Y/E = 5.15022 % +========Time details of each equation======= +rhoEqn Time = 0.000271 s +rhoEqn assamble = 0.000215 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001137 s +UEqn assamble = 0.0006 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000537 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001735 s +YEqn assamble = 0.000644 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000174 s +YEqn correct boundary = 0 s +EEqn Time = 0.000446 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 7.3 s ClockTime = 8 s +Courant Number mean: 0.00016313 max: 0.0137703 +Time = 0.000185 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 43 new parcels + +Cloud: sprayCloud + Current number of parcels = 1867 + Current mass in system = 2.74675e-10 + Linear momentum = (1.42682e-11 -3.03196e-09 0) + |Linear momentum| = 3.032e-09 + Linear kinetic energy = 1.79166e-08 + model1: + number of parcels added = 1867 + mass introduced = 2.75576e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.146, 516.489 + Mass transfer phase change = 9.00857e-13 + D10, D32, Dmax (mu) = 44.1298, 81.2011, 149.142 + Liquid penetration 95% mass (m) = 0.0013121 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0133749, Final residual = 1.95878e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0201466, Final residual = 4.59608e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0084345, Final residual = 7.24549e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00868351, Final residual = 5.18126e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00934922, Final residual = 2.67711e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00934924, Final residual = 2.68129e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00823316, Final residual = 5.8264e-07, No Iterations 1 +min/max(T) = 662.718, 807.693 +GAMG: Solving for p, Initial residual = 0.0222339, Final residual = 0.00016045, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.57502e-07, global = 3.4115e-07, cumulative = 2.09609e-05 +GAMG: Solving for p, Initial residual = 0.00015846, Final residual = 2.75358e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.36173e-07, global = 3.36136e-07, cumulative = 2.1297e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000377603, Final residual = 2.20198e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00876664, Final residual = 7.96788e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095833 s +other Time = 0 s +rho Equations = 0.00016 s +U Equations = 0.001279 s +Y Equations = 0.00236666 s +E Equations = 0.000612 s +p Equations = 0.00223 s +calculate parcels = 1.2971 s +chemistry correctThermo = 0.00279 s +turbulence correct = 0.00102 s +combustion correct(in Y) = 0.0851853 s +percentage of chemistry = 88.8894 % +percentage of rho/U/Y/E = 4.60975 % +========Time details of each equation======= +rhoEqn Time = 0.000303 s +rhoEqn assamble = 0.000236 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001279 s +UEqn assamble = 0.000746 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000533 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001606 s +YEqn assamble = 0.000619 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000121 s +YEqn correct boundary = 0 s +EEqn Time = 0.000458 s +EEqn assamble = 0.000327 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000131 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 7.44 s ClockTime = 8 s +Courant Number mean: 0.000166693 max: 0.0140239 +Time = 0.0001875 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 45 new parcels + +Cloud: sprayCloud + Current number of parcels = 1912 + Current mass in system = 2.79711e-10 + Linear momentum = (1.30995e-11 -3.08863e-09 0) + |Linear momentum| = 3.08866e-09 + Linear kinetic energy = 1.82435e-08 + model1: + number of parcels added = 1912 + mass introduced = 2.80642e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.129, 516.582 + Mass transfer phase change = 9.30389e-13 + D10, D32, Dmax (mu) = 44.0255, 80.9971, 148.982 + Liquid penetration 95% mass (m) = 0.00133759 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0129407, Final residual = 1.71926e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0202498, Final residual = 4.61918e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00857974, Final residual = 7.47516e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0085913, Final residual = 5.28608e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0092451, Final residual = 2.68665e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00924513, Final residual = 2.69085e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00809146, Final residual = 5.75013e-07, No Iterations 1 +min/max(T) = 659.152, 807.896 +GAMG: Solving for p, Initial residual = 0.0226173, Final residual = 0.000167302, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.6276e-07, global = 3.44861e-07, cumulative = 2.16419e-05 +GAMG: Solving for p, Initial residual = 0.000167239, Final residual = 2.0512e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.40414e-07, global = 3.40388e-07, cumulative = 2.19823e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000378738, Final residual = 2.23382e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00870895, Final residual = 7.96351e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.093169 s +other Time = 0 s +rho Equations = 0.000169 s +U Equations = 0.001214 s +Y Equations = 0.00251598 s +E Equations = 0.000679 s +p Equations = 0.002656 s +calculate parcels = 1.33888 s +chemistry correctThermo = 0.002815 s +turbulence correct = 0.000939 s +combustion correct(in Y) = 0.081971 s +percentage of chemistry = 87.981 % +percentage of rho/U/Y/E = 4.91363 % +========Time details of each equation======= +rhoEqn Time = 0.000334 s +rhoEqn assamble = 0.000262 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001213 s +UEqn assamble = 0.000711 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000502 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001867 s +YEqn assamble = 0.000702 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000187 s +YEqn correct boundary = 0 s +EEqn Time = 0.00051 s +EEqn assamble = 0.000388 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000122 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 7.57 s ClockTime = 8 s +Courant Number mean: 0.000170292 max: 0.0142545 +Time = 0.00019 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 1958 + Current mass in system = 2.84835e-10 + Linear momentum = (1.32604e-11 -3.14618e-09 0) + |Linear momentum| = 3.14621e-09 + Linear kinetic energy = 1.8575e-08 + model1: + number of parcels added = 1958 + mass introduced = 2.85795e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.138, 516.676 + Mass transfer phase change = 9.60342e-13 + D10, D32, Dmax (mu) = 44.1876, 80.935, 148.799 + Liquid penetration 95% mass (m) = 0.00136366 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0123714, Final residual = 1.52171e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0203763, Final residual = 4.6504e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00844688, Final residual = 7.40753e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00847913, Final residual = 5.21895e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0091358, Final residual = 2.69535e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00913583, Final residual = 2.69954e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00796489, Final residual = 5.64815e-07, No Iterations 1 +min/max(T) = 655.721, 808.099 +GAMG: Solving for p, Initial residual = 0.0229983, Final residual = 0.000191494, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.6956e-07, global = 3.49948e-07, cumulative = 2.23322e-05 +GAMG: Solving for p, Initial residual = 0.000191287, Final residual = 3.70562e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.45288e-07, global = 3.4524e-07, cumulative = 2.26775e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000380168, Final residual = 2.2692e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00865505, Final residual = 7.96576e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.090529 s +other Time = 0 s +rho Equations = 0.000136 s +U Equations = 0.001023 s +Y Equations = 0.00234938 s +E Equations = 0.00062 s +p Equations = 0.002212 s +calculate parcels = 1.38929 s +chemistry correctThermo = 0.002792 s +turbulence correct = 0.001023 s +combustion correct(in Y) = 0.0802026 s +percentage of chemistry = 88.5933 % +percentage of rho/U/Y/E = 4.56029 % +========Time details of each equation======= +rhoEqn Time = 0.000279 s +rhoEqn assamble = 0.00022 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001023 s +UEqn assamble = 0.000594 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000429 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001773 s +YEqn assamble = 0.000654 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000221 s +YEqn correct boundary = 0 s +EEqn Time = 0.000464 s +EEqn assamble = 0.000333 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000131 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 7.71 s ClockTime = 8 s +Courant Number mean: 0.000173962 max: 0.0144856 +Time = 0.0001925 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 2004 + Current mass in system = 2.89937e-10 + Linear momentum = (1.43995e-11 -3.20312e-09 0) + |Linear momentum| = 3.20316e-09 + Linear kinetic energy = 1.89008e-08 + model1: + number of parcels added = 2004 + mass introduced = 2.90927e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.142, 516.77 + Mass transfer phase change = 9.90769e-13 + D10, D32, Dmax (mu) = 44.3392, 80.7674, 148.595 + Liquid penetration 95% mass (m) = 0.00138884 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0124129, Final residual = 1.47065e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0204985, Final residual = 4.67729e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00839282, Final residual = 7.42907e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00841072, Final residual = 5.19977e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00903849, Final residual = 2.70359e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00903852, Final residual = 2.70778e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00784971, Final residual = 5.56373e-07, No Iterations 1 +min/max(T) = 652.412, 808.302 +GAMG: Solving for p, Initial residual = 0.0231421, Final residual = 0.000161497, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.71457e-07, global = 3.55261e-07, cumulative = 2.30327e-05 +GAMG: Solving for p, Initial residual = 0.000161051, Final residual = 3.27583e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.50748e-07, global = 3.50706e-07, cumulative = 2.33834e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000381898, Final residual = 2.30747e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00860469, Final residual = 7.97326e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.088453 s +other Time = 0 s +rho Equations = 0.000206 s +U Equations = 0.001198 s +Y Equations = 0.00221959 s +E Equations = 0.00049 s +p Equations = 0.001788 s +calculate parcels = 1.43277 s +chemistry correctThermo = 0.001972 s +turbulence correct = 0.000852 s +combustion correct(in Y) = 0.0795434 s +percentage of chemistry = 89.9273 % +percentage of rho/U/Y/E = 4.6506 % +========Time details of each equation======= +rhoEqn Time = 0.000323 s +rhoEqn assamble = 0.000257 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001196 s +UEqn assamble = 0.000704 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000492 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00156 s +YEqn assamble = 0.000615 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.9e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000368 s +EEqn assamble = 0.000275 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 7.84 s ClockTime = 8 s +Courant Number mean: 0.000177666 max: 0.0147103 +Time = 0.000195 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 28 new parcels + +Cloud: sprayCloud + Current number of parcels = 2032 + Current mass in system = 2.93016e-10 + Linear momentum = (1.36693e-11 -3.23235e-09 0) + |Linear momentum| = 3.23238e-09 + Linear kinetic energy = 1.90358e-08 + model1: + number of parcels added = 2032 + mass introduced = 2.94038e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.147, 516.861 + Mass transfer phase change = 1.02162e-12 + D10, D32, Dmax (mu) = 44.4678, 80.588, 148.554 + Liquid penetration 95% mass (m) = 0.00141433 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0125586, Final residual = 1.47721e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0206357, Final residual = 4.70085e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00830892, Final residual = 7.42498e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00832988, Final residual = 5.16411e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00894656, Final residual = 2.71249e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00894659, Final residual = 2.71668e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00768581, Final residual = 5.44477e-07, No Iterations 1 +min/max(T) = 649.221, 808.503 +GAMG: Solving for p, Initial residual = 0.0235899, Final residual = 0.000179025, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.79835e-07, global = 3.595e-07, cumulative = 2.37429e-05 +GAMG: Solving for p, Initial residual = 0.00017894, Final residual = 3.94982e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.55602e-07, global = 3.55548e-07, cumulative = 2.40985e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000384019, Final residual = 2.34951e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00855896, Final residual = 7.987e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094523 s +other Time = 0 s +rho Equations = 0.000147 s +U Equations = 0.001153 s +Y Equations = 0.0023878 s +E Equations = 0.000599 s +p Equations = 0.002219 s +calculate parcels = 1.47574 s +chemistry correctThermo = 0.002822 s +turbulence correct = 0.001022 s +combustion correct(in Y) = 0.0839912 s +percentage of chemistry = 88.858 % +percentage of rho/U/Y/E = 4.53519 % +========Time details of each equation======= +rhoEqn Time = 0.000286 s +rhoEqn assamble = 0.000225 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001152 s +UEqn assamble = 0.000667 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000485 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001735 s +YEqn assamble = 0.000662 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000177 s +YEqn correct boundary = 0 s +EEqn Time = 0.000444 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 7.98 s ClockTime = 8 s +Courant Number mean: 0.000181314 max: 0.0149052 +Time = 0.0001975 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 39 new parcels + +Cloud: sprayCloud + Current number of parcels = 2071 + Current mass in system = 2.97259e-10 + Linear momentum = (1.63968e-11 -3.27705e-09 0) + |Linear momentum| = 3.27709e-09 + Linear kinetic energy = 1.92752e-08 + model1: + number of parcels added = 2071 + mass introduced = 2.98312e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.142, 516.947 + Mass transfer phase change = 1.05308e-12 + D10, D32, Dmax (mu) = 43.9649, 80.2772, 148.558 + Liquid penetration 95% mass (m) = 0.00143932 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0121236, Final residual = 1.53016e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0207272, Final residual = 4.73625e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00822103, Final residual = 7.42588e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00824269, Final residual = 5.1297e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00884794, Final residual = 2.72245e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00884797, Final residual = 2.72664e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00760367, Final residual = 5.4035e-07, No Iterations 1 +min/max(T) = 646.115, 808.705 +GAMG: Solving for p, Initial residual = 0.0241927, Final residual = 0.000171734, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.83929e-07, global = 3.67159e-07, cumulative = 2.44656e-05 +GAMG: Solving for p, Initial residual = 0.00017141, Final residual = 3.65331e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.62724e-07, global = 3.62677e-07, cumulative = 2.48283e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000386422, Final residual = 2.39419e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00851516, Final residual = 8.00419e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.087549 s +other Time = 0 s +rho Equations = 0.000144 s +U Equations = 0.001114 s +Y Equations = 0.00272047 s +E Equations = 0.000726 s +p Equations = 0.002392 s +calculate parcels = 1.51943 s +chemistry correctThermo = 0.002875 s +turbulence correct = 0.001047 s +combustion correct(in Y) = 0.0763375 s +percentage of chemistry = 87.1941 % +percentage of rho/U/Y/E = 5.37352 % +========Time details of each equation======= +rhoEqn Time = 0.000298 s +rhoEqn assamble = 0.000237 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001113 s +UEqn assamble = 0.000592 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000521 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002003 s +YEqn assamble = 0.000739 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000202 s +YEqn correct boundary = 0 s +EEqn Time = 0.000541 s +EEqn assamble = 0.000395 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000146 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 8.11 s ClockTime = 8 s +Courant Number mean: 0.000184939 max: 0.0151329 +Time = 0.0002 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 38 new parcels + +Cloud: sprayCloud + Current number of parcels = 2109 + Current mass in system = 3.01359e-10 + Linear momentum = (1.74422e-11 -3.31961e-09 0) + |Linear momentum| = 3.31965e-09 + Linear kinetic energy = 1.94985e-08 + model1: + number of parcels added = 2109 + mass introduced = 3.02444e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.139, 517.026 + Mass transfer phase change = 1.08511e-12 + D10, D32, Dmax (mu) = 44.1259, 80.1523, 148.562 + Liquid penetration 95% mass (m) = 0.00146559 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0121382, Final residual = 1.51016e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0208075, Final residual = 4.74763e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00811799, Final residual = 7.41307e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00815498, Final residual = 5.08419e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00876111, Final residual = 2.72591e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00876113, Final residual = 2.7301e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0074965, Final residual = 5.3814e-07, No Iterations 1 +min/max(T) = 643.084, 808.904 +GAMG: Solving for p, Initial residual = 0.0248186, Final residual = 0.000169996, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.89214e-07, global = 3.72675e-07, cumulative = 2.5201e-05 +GAMG: Solving for p, Initial residual = 0.000170029, Final residual = 1.96542e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.69158e-07, global = 3.69135e-07, cumulative = 2.55701e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000389294, Final residual = 2.44336e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00847683, Final residual = 8.0283e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.086654 s +other Time = 0 s +rho Equations = 0.000137 s +U Equations = 0.00106 s +Y Equations = 0.00215025 s +E Equations = 0.000508 s +p Equations = 0.002016 s +calculate parcels = 1.56404 s +chemistry correctThermo = 0.002001 s +turbulence correct = 0.000861 s +combustion correct(in Y) = 0.0777638 s +percentage of chemistry = 89.7405 % +percentage of rho/U/Y/E = 4.44901 % +========Time details of each equation======= +rhoEqn Time = 0.000259 s +rhoEqn assamble = 0.000206 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001058 s +UEqn assamble = 0.000624 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000434 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001512 s +YEqn assamble = 0.000563 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000111 s +YEqn correct boundary = 0 s +EEqn Time = 0.000382 s +EEqn assamble = 0.000285 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.7e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 8.3 s ClockTime = 9 s +Courant Number mean: 0.00018848 max: 0.0153337 +Time = 0.0002025 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 2153 + Current mass in system = 3.0607e-10 + Linear momentum = (1.87438e-11 -3.37008e-09 0) + |Linear momentum| = 3.37013e-09 + Linear kinetic energy = 1.97754e-08 + model1: + number of parcels added = 2153 + mass introduced = 3.07188e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.142, 517.094 + Mass transfer phase change = 1.11769e-12 + D10, D32, Dmax (mu) = 44.343, 80.0836, 148.566 + Liquid penetration 95% mass (m) = 0.00149129 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0116964, Final residual = 9.76064e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0208572, Final residual = 4.76781e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00805624, Final residual = 7.44003e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00808495, Final residual = 5.05394e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00867214, Final residual = 2.73284e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00867217, Final residual = 2.73703e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0073866, Final residual = 5.41396e-07, No Iterations 1 +min/max(T) = 640.161, 809.102 +GAMG: Solving for p, Initial residual = 0.0256498, Final residual = 0.000241384, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.0605e-07, global = 3.80751e-07, cumulative = 2.59509e-05 +GAMG: Solving for p, Initial residual = 0.000243376, Final residual = 2.60754e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.75582e-07, global = 3.75549e-07, cumulative = 2.63264e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000392634, Final residual = 2.49508e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00844249, Final residual = 8.05405e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.066503 s +other Time = 1e-06 s +rho Equations = 0.000152 s +U Equations = 0.001277 s +Y Equations = 0.00221804 s +E Equations = 0.0005 s +p Equations = 0.001833 s +calculate parcels = 1.60137 s +chemistry correctThermo = 0.001962 s +turbulence correct = 0.000864 s +combustion correct(in Y) = 0.057526 s +percentage of chemistry = 86.5013 % +percentage of rho/U/Y/E = 6.23586 % +========Time details of each equation======= +rhoEqn Time = 0.000273 s +rhoEqn assamble = 0.000218 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001275 s +UEqn assamble = 0.000872 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000403 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001598 s +YEqn assamble = 0.000632 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000124 s +YEqn correct boundary = 0 s +EEqn Time = 0.000374 s +EEqn assamble = 0.000278 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 8.4 s ClockTime = 9 s +Courant Number mean: 0.000191834 max: 0.0155034 +Time = 0.000205 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 39 new parcels + +Cloud: sprayCloud + Current number of parcels = 2192 + Current mass in system = 3.1022e-10 + Linear momentum = (1.80389e-11 -3.41277e-09 0) + |Linear momentum| = 3.41281e-09 + Linear kinetic energy = 1.9998e-08 + model1: + number of parcels added = 2192 + mass introduced = 3.11371e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.141, 517.151 + Mass transfer phase change = 1.15111e-12 + D10, D32, Dmax (mu) = 44.5288, 79.9548, 148.571 + Liquid penetration 95% mass (m) = 0.00151662 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0103276, Final residual = 8.7545e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.020742, Final residual = 4.78377e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00800345, Final residual = 7.42702e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00802036, Final residual = 4.97433e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00858738, Final residual = 2.72713e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0085874, Final residual = 2.73129e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00736922, Final residual = 5.33693e-07, No Iterations 1 +min/max(T) = 637.495, 809.303 +GAMG: Solving for p, Initial residual = 0.0274613, Final residual = 0.000434786, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.32961e-07, global = 3.85358e-07, cumulative = 2.67118e-05 +GAMG: Solving for p, Initial residual = 0.000440267, Final residual = 4.71605e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.85184e-07, global = 3.85133e-07, cumulative = 2.70969e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000396135, Final residual = 2.54528e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00840651, Final residual = 8.07189e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.068259 s +other Time = 1e-06 s +rho Equations = 0.000151 s +U Equations = 0.001036 s +Y Equations = 0.00205317 s +E Equations = 0.00049 s +p Equations = 0.001794 s +calculate parcels = 1.63605 s +chemistry correctThermo = 0.001961 s +turbulence correct = 0.000897 s +combustion correct(in Y) = 0.0596998 s +percentage of chemistry = 87.4607 % +percentage of rho/U/Y/E = 5.46473 % +========Time details of each equation======= +rhoEqn Time = 0.000269 s +rhoEqn assamble = 0.000213 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001035 s +UEqn assamble = 0.000659 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000376 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001455 s +YEqn assamble = 0.000544 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000111 s +YEqn correct boundary = 0 s +EEqn Time = 0.00037 s +EEqn assamble = 0.000275 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 8.5 s ClockTime = 9 s +Courant Number mean: 0.000194975 max: 0.0156617 +Time = 0.0002075 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 27 new parcels + +Cloud: sprayCloud + Current number of parcels = 2219 + Current mass in system = 3.1306e-10 + Linear momentum = (1.7628e-11 -3.43778e-09 0) + |Linear momentum| = 3.43782e-09 + Linear kinetic energy = 2.00998e-08 + model1: + number of parcels added = 2219 + mass introduced = 3.14245e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.136, 517.194 + Mass transfer phase change = 1.18525e-12 + D10, D32, Dmax (mu) = 44.6338, 79.8512, 148.575 + Liquid penetration 95% mass (m) = 0.00154309 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00866923, Final residual = 6.93178e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0206215, Final residual = 4.78446e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00798324, Final residual = 7.41877e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.007971, Final residual = 4.94319e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00850196, Final residual = 2.70143e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00850199, Final residual = 2.70554e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00740519, Final residual = 5.28591e-07, No Iterations 1 +min/max(T) = 635.081, 809.502 +GAMG: Solving for p, Initial residual = 0.0283471, Final residual = 0.000403748, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.35582e-07, global = 4.02607e-07, cumulative = 2.74995e-05 +GAMG: Solving for p, Initial residual = 0.000412097, Final residual = 5.08558e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.936e-07, global = 3.93546e-07, cumulative = 2.78931e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000399966, Final residual = 2.59688e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00837217, Final residual = 8.08911e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.088354 s +other Time = 1e-06 s +rho Equations = 0.000158 s +U Equations = 0.001181 s +Y Equations = 0.00212209 s +E Equations = 0.000538 s +p Equations = 0.001842 s +calculate parcels = 1.67314 s +chemistry correctThermo = 0.00201 s +turbulence correct = 0.000832 s +combustion correct(in Y) = 0.0794889 s +percentage of chemistry = 89.9664 % +percentage of rho/U/Y/E = 4.52621 % +========Time details of each equation======= +rhoEqn Time = 0.000277 s +rhoEqn assamble = 0.000218 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001179 s +UEqn assamble = 0.000735 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000444 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001424 s +YEqn assamble = 0.000555 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 7.3e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000419 s +EEqn assamble = 0.000281 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000138 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 8.63 s ClockTime = 9 s +Courant Number mean: 0.00019789 max: 0.0157704 +Time = 0.00021 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 36 new parcels + +Cloud: sprayCloud + Current number of parcels = 2255 + Current mass in system = 3.16803e-10 + Linear momentum = (1.71168e-11 -3.47469e-09 0) + |Linear momentum| = 3.47473e-09 + Linear kinetic energy = 2.02822e-08 + model1: + number of parcels added = 2255 + mass introduced = 3.18024e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.15, 517.217 + Mass transfer phase change = 1.22019e-12 + D10, D32, Dmax (mu) = 44.8047, 79.7824, 148.579 + Liquid penetration 95% mass (m) = 0.00156939 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00768951, Final residual = 6.03657e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0205373, Final residual = 4.80126e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00794697, Final residual = 7.32707e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00791739, Final residual = 4.83988e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00842503, Final residual = 2.67983e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00842504, Final residual = 2.68395e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00744737, Final residual = 5.21237e-07, No Iterations 1 +min/max(T) = 632.902, 809.702 +GAMG: Solving for p, Initial residual = 0.0289149, Final residual = 0.000283689, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.28699e-07, global = 4.10957e-07, cumulative = 2.8304e-05 +GAMG: Solving for p, Initial residual = 0.000285685, Final residual = 4.936e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.0271e-07, global = 4.0266e-07, cumulative = 2.87067e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000404028, Final residual = 2.64948e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00833789, Final residual = 8.1048e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.082095 s +other Time = 0 s +rho Equations = 0.000164 s +U Equations = 0.001136 s +Y Equations = 0.00240166 s +E Equations = 0.0006 s +p Equations = 0.002318 s +calculate parcels = 1.71355 s +chemistry correctThermo = 0.002778 s +turbulence correct = 0.001011 s +combustion correct(in Y) = 0.0714993 s +percentage of chemistry = 87.0934 % +percentage of rho/U/Y/E = 5.23986 % +========Time details of each equation======= +rhoEqn Time = 0.000312 s +rhoEqn assamble = 0.000248 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001135 s +UEqn assamble = 0.0007 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000435 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001763 s +YEqn assamble = 0.00064 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000184 s +YEqn correct boundary = 0 s +EEqn Time = 0.000443 s +EEqn assamble = 0.000331 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 8.75 s ClockTime = 9 s +Courant Number mean: 0.000200716 max: 0.0158787 +Time = 0.0002125 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 2301 + Current mass in system = 3.2155e-10 + Linear momentum = (1.60408e-11 -3.5247e-09 0) + |Linear momentum| = 3.52474e-09 + Linear kinetic energy = 2.0552e-08 + model1: + number of parcels added = 2301 + mass introduced = 3.22806e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.144, 517.219 + Mass transfer phase change = 1.25601e-12 + D10, D32, Dmax (mu) = 44.8545, 79.5483, 148.583 + Liquid penetration 95% mass (m) = 0.00159472 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00805847, Final residual = 6.80082e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0204477, Final residual = 4.81342e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00791524, Final residual = 7.21756e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00787168, Final residual = 4.77144e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00835937, Final residual = 2.67694e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00835938, Final residual = 2.68102e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00747339, Final residual = 5.19315e-07, No Iterations 1 +min/max(T) = 630.923, 809.899 +GAMG: Solving for p, Initial residual = 0.0302001, Final residual = 0.00040018, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.49101e-07, global = 4.24872e-07, cumulative = 2.91315e-05 +GAMG: Solving for p, Initial residual = 0.000404006, Final residual = 7.07309e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.13026e-07, global = 4.12958e-07, cumulative = 2.95445e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.00040824, Final residual = 2.70221e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00830268, Final residual = 8.11855e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.086885 s +other Time = 0 s +rho Equations = 0.000138 s +U Equations = 0.000943 s +Y Equations = 0.00194411 s +E Equations = 0.000483 s +p Equations = 0.001814 s +calculate parcels = 1.76185 s +chemistry correctThermo = 0.002004 s +turbulence correct = 0.000826 s +combustion correct(in Y) = 0.0785649 s +percentage of chemistry = 90.424 % +percentage of rho/U/Y/E = 4.03764 % +========Time details of each equation======= +rhoEqn Time = 0.000257 s +rhoEqn assamble = 0.000206 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000942 s +UEqn assamble = 0.000585 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000357 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001385 s +YEqn assamble = 0.000521 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00013 s +YEqn correct boundary = 0 s +EEqn Time = 0.000364 s +EEqn assamble = 0.000272 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 8.89 s ClockTime = 9 s +Courant Number mean: 0.000203606 max: 0.0160008 +Time = 0.000215 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 35 new parcels + +Cloud: sprayCloud + Current number of parcels = 2336 + Current mass in system = 3.25135e-10 + Linear momentum = (1.53011e-11 -3.55912e-09 0) + |Linear momentum| = 3.55915e-09 + Linear kinetic energy = 2.07157e-08 + model1: + number of parcels added = 2336 + mass introduced = 3.26428e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.138, 517.2 + Mass transfer phase change = 1.29256e-12 + D10, D32, Dmax (mu) = 44.9683, 79.4796, 148.588 + Liquid penetration 95% mass (m) = 0.00162043 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00981701, Final residual = 8.43778e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.020448, Final residual = 4.80172e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00789617, Final residual = 7.10477e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00783415, Final residual = 4.70004e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00829787, Final residual = 2.66081e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00829787, Final residual = 2.66484e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0075326, Final residual = 5.18332e-07, No Iterations 1 +min/max(T) = 629.132, 810.093 +GAMG: Solving for p, Initial residual = 0.0324298, Final residual = 0.000386825, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.58847e-07, global = 4.27445e-07, cumulative = 2.99719e-05 +GAMG: Solving for p, Initial residual = 0.000391909, Final residual = 5.70096e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.2127e-07, global = 4.21214e-07, cumulative = 3.03932e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.00041285, Final residual = 2.75998e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00827048, Final residual = 8.1396e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.07713 s +other Time = 1e-06 s +rho Equations = 0.000133 s +U Equations = 0.000989 s +Y Equations = 0.00237169 s +E Equations = 0.000627 s +p Equations = 0.002194 s +calculate parcels = 1.7985 s +chemistry correctThermo = 0.002783 s +turbulence correct = 0.000994 s +combustion correct(in Y) = 0.0668733 s +percentage of chemistry = 86.7021 % +percentage of rho/U/Y/E = 5.34252 % +========Time details of each equation======= +rhoEqn Time = 0.000276 s +rhoEqn assamble = 0.00022 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000988 s +UEqn assamble = 0.000621 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000367 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001812 s +YEqn assamble = 0.000666 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000258 s +YEqn correct boundary = 0 s +EEqn Time = 0.000468 s +EEqn assamble = 0.000352 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 9 s ClockTime = 9 s +Courant Number mean: 0.000206601 max: 0.0160722 +Time = 0.0002175 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 2380 + Current mass in system = 3.29605e-10 + Linear momentum = (1.59516e-11 -3.60509e-09 0) + |Linear momentum| = 3.60512e-09 + Linear kinetic energy = 2.09565e-08 + model1: + number of parcels added = 2380 + mass introduced = 3.30935e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.132, 517.162 + Mass transfer phase change = 1.32983e-12 + D10, D32, Dmax (mu) = 45.15, 79.5142, 148.592 + Liquid penetration 95% mass (m) = 0.00164487 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0108241, Final residual = 9.64824e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0204871, Final residual = 4.81431e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00787264, Final residual = 7.00096e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0077938, Final residual = 4.64101e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00823659, Final residual = 2.64667e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00823659, Final residual = 2.65064e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0075776, Final residual = 5.18793e-07, No Iterations 1 +min/max(T) = 627.491, 810.289 +GAMG: Solving for p, Initial residual = 0.0339974, Final residual = 0.000373488, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.66748e-07, global = 4.34465e-07, cumulative = 3.08276e-05 +GAMG: Solving for p, Initial residual = 0.000376867, Final residual = 6.65066e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.29687e-07, global = 4.29619e-07, cumulative = 3.12572e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000417853, Final residual = 2.82593e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00824044, Final residual = 8.17102e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.088108 s +other Time = 1e-06 s +rho Equations = 0.000186 s +U Equations = 0.001167 s +Y Equations = 0.0023646 s +E Equations = 0.0006 s +p Equations = 0.00216 s +calculate parcels = 1.8414 s +chemistry correctThermo = 0.002776 s +turbulence correct = 0.000963 s +combustion correct(in Y) = 0.0777024 s +percentage of chemistry = 88.19 % +percentage of rho/U/Y/E = 4.90035 % +========Time details of each equation======= +rhoEqn Time = 0.000322 s +rhoEqn assamble = 0.00025 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001167 s +UEqn assamble = 0.000729 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000438 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001712 s +YEqn assamble = 0.000648 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000184 s +YEqn correct boundary = 0 s +EEqn Time = 0.000445 s +EEqn assamble = 0.000331 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 9.13 s ClockTime = 10 s +Courant Number mean: 0.000209719 max: 0.0161342 +Time = 0.00022 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 41 new parcels + +Cloud: sprayCloud + Current number of parcels = 2421 + Current mass in system = 3.33744e-10 + Linear momentum = (1.426e-11 -3.64652e-09 0) + |Linear momentum| = 3.64654e-09 + Linear kinetic energy = 2.11658e-08 + model1: + number of parcels added = 2421 + mass introduced = 3.35112e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.141, 517.105 + Mass transfer phase change = 1.36783e-12 + D10, D32, Dmax (mu) = 45.3107, 79.4637, 148.596 + Liquid penetration 95% mass (m) = 0.00167012 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.011641, Final residual = 1.49305e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0205012, Final residual = 4.82352e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00781031, Final residual = 6.85707e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0077376, Final residual = 4.56723e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00818098, Final residual = 2.63803e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00818098, Final residual = 2.64195e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00758118, Final residual = 5.1669e-07, No Iterations 1 +min/max(T) = 625.996, 810.488 +GAMG: Solving for p, Initial residual = 0.03573, Final residual = 0.000354023, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.72144e-07, global = 4.43124e-07, cumulative = 3.17004e-05 +GAMG: Solving for p, Initial residual = 0.000358132, Final residual = 5.87961e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.37959e-07, global = 4.37901e-07, cumulative = 3.21383e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000423139, Final residual = 2.90134e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00821122, Final residual = 8.21338e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.091645 s +other Time = 0 s +rho Equations = 0.000196 s +U Equations = 0.001294 s +Y Equations = 0.00326243 s +E Equations = 0.000959 s +p Equations = 0.002162 s +calculate parcels = 1.89025 s +chemistry correctThermo = 0.003981 s +turbulence correct = 0.000966 s +combustion correct(in Y) = 0.0786066 s +percentage of chemistry = 85.7729 % +percentage of rho/U/Y/E = 6.23213 % +========Time details of each equation======= +rhoEqn Time = 0.000332 s +rhoEqn assamble = 0.000265 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001294 s +UEqn assamble = 0.000775 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000519 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002559 s +YEqn assamble = 0.001033 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000409 s +YEqn correct boundary = 0 s +EEqn Time = 0.000725 s +EEqn assamble = 0.000529 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000196 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 9.27 s ClockTime = 10 s +Courant Number mean: 0.000212937 max: 0.0161992 +Time = 0.0002225 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 58 new parcels + +Cloud: sprayCloud + Current number of parcels = 2479 + Current mass in system = 3.39572e-10 + Linear momentum = (1.38707e-11 -3.70981e-09 0) + |Linear momentum| = 3.70984e-09 + Linear kinetic energy = 2.15192e-08 + model1: + number of parcels added = 2479 + mass introduced = 3.40979e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.14, 517.03 + Mass transfer phase change = 1.40702e-12 + D10, D32, Dmax (mu) = 38.4733, 79.1576, 148.601 + Liquid penetration 95% mass (m) = 0.00169433 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0120949, Final residual = 1.60883e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0204332, Final residual = 4.83242e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00763607, Final residual = 6.71434e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00768599, Final residual = 4.41141e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0081297, Final residual = 2.61976e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00812971, Final residual = 2.62361e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00749199, Final residual = 4.95352e-07, No Iterations 1 +min/max(T) = 624.66, 810.687 +GAMG: Solving for p, Initial residual = 0.0393424, Final residual = 0.000835878, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.21439e-07, global = 4.756e-07, cumulative = 3.26139e-05 +GAMG: Solving for p, Initial residual = 0.000861151, Final residual = 3.27772e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.518e-07, global = 4.51771e-07, cumulative = 3.30656e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.00042801, Final residual = 2.97983e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00817465, Final residual = 8.25546e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095241 s +other Time = 0 s +rho Equations = 0.000185 s +U Equations = 0.001194 s +Y Equations = 0.00233375 s +E Equations = 0.000596 s +p Equations = 0.002371 s +calculate parcels = 1.94228 s +chemistry correctThermo = 0.0028 s +turbulence correct = 0.001087 s +combustion correct(in Y) = 0.0844783 s +percentage of chemistry = 88.6995 % +percentage of rho/U/Y/E = 4.52405 % +========Time details of each equation======= +rhoEqn Time = 0.000333 s +rhoEqn assamble = 0.000245 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001193 s +UEqn assamble = 0.000693 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.0005 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001685 s +YEqn assamble = 0.000647 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000166 s +YEqn correct boundary = 0 s +EEqn Time = 0.000442 s +EEqn assamble = 0.000329 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 9.42 s ClockTime = 10 s +Courant Number mean: 0.000216403 max: 0.0163716 +Time = 0.000225 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 43 new parcels + +Cloud: sprayCloud + Current number of parcels = 2522 + Current mass in system = 3.43887e-10 + Linear momentum = (1.50196e-11 -3.75294e-09 0) + |Linear momentum| = 3.75297e-09 + Linear kinetic energy = 2.1737e-08 + model1: + number of parcels added = 2522 + mass introduced = 3.45335e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.134, 516.936 + Mass transfer phase change = 1.44709e-12 + D10, D32, Dmax (mu) = 38.5971, 78.9944, 148.605 + Liquid penetration 95% mass (m) = 0.00171891 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0146193, Final residual = 1.82764e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0206332, Final residual = 4.80723e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00758738, Final residual = 6.70691e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00763657, Final residual = 4.34e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0080674, Final residual = 2.58171e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0080674, Final residual = 2.58549e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0075027, Final residual = 4.97615e-07, No Iterations 1 +min/max(T) = 623.467, 810.878 +GAMG: Solving for p, Initial residual = 0.0433407, Final residual = 0.000637111, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.10676e-07, global = 4.73141e-07, cumulative = 3.35388e-05 +GAMG: Solving for p, Initial residual = 0.000653398, Final residual = 9.92959e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.61866e-07, global = 4.61787e-07, cumulative = 3.40006e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000433727, Final residual = 3.06767e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00814663, Final residual = 8.30775e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.088584 s +other Time = 1e-06 s +rho Equations = 0.000137 s +U Equations = 0.001051 s +Y Equations = 0.00233073 s +E Equations = 0.000605 s +p Equations = 0.002239 s +calculate parcels = 1.98147 s +chemistry correctThermo = 0.002797 s +turbulence correct = 0.000986 s +combustion correct(in Y) = 0.0782013 s +percentage of chemistry = 88.2792 % +percentage of rho/U/Y/E = 4.65516 % +========Time details of each equation======= +rhoEqn Time = 0.000288 s +rhoEqn assamble = 0.000226 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00105 s +UEqn assamble = 0.000619 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000431 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001771 s +YEqn assamble = 0.00066 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000226 s +YEqn correct boundary = 0 s +EEqn Time = 0.000448 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 9.55 s ClockTime = 10 s +Courant Number mean: 0.00021976 max: 0.0164055 +Time = 0.0002275 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 2570 + Current mass in system = 3.48679e-10 + Linear momentum = (1.39836e-11 -3.80223e-09 0) + |Linear momentum| = 3.80226e-09 + Linear kinetic energy = 2.19946e-08 + model1: + number of parcels added = 2570 + mass introduced = 3.50167e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.148, 516.826 + Mass transfer phase change = 1.48802e-12 + D10, D32, Dmax (mu) = 38.7986, 79.0148, 148.609 + Liquid penetration 95% mass (m) = 0.00174438 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0143178, Final residual = 1.99793e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0207334, Final residual = 4.84293e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00748253, Final residual = 6.57438e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00759332, Final residual = 4.21113e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00800556, Final residual = 2.54885e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00800557, Final residual = 2.55256e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00751151, Final residual = 4.9375e-07, No Iterations 1 +min/max(T) = 622.43, 811.078 +GAMG: Solving for p, Initial residual = 0.045231, Final residual = 0.000529313, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.17155e-07, global = 4.81653e-07, cumulative = 3.44822e-05 +GAMG: Solving for p, Initial residual = 0.000542254, Final residual = 2.04995e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.71807e-07, global = 4.7179e-07, cumulative = 3.4954e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000439958, Final residual = 3.16634e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00812178, Final residual = 8.37042e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.075143 s +other Time = 0 s +rho Equations = 0.000162 s +U Equations = 0.001326 s +Y Equations = 0.00211428 s +E Equations = 0.000503 s +p Equations = 0.001997 s +calculate parcels = 2.03675 s +chemistry correctThermo = 0.001985 s +turbulence correct = 0.000806 s +combustion correct(in Y) = 0.0660567 s +percentage of chemistry = 87.908 % +percentage of rho/U/Y/E = 5.4633 % +========Time details of each equation======= +rhoEqn Time = 0.00028 s +rhoEqn assamble = 0.00022 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001325 s +UEqn assamble = 0.000892 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000433 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001559 s +YEqn assamble = 0.000569 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000176 s +YEqn correct boundary = 0 s +EEqn Time = 0.00038 s +EEqn assamble = 0.000286 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 9.68 s ClockTime = 10 s +Courant Number mean: 0.000223037 max: 0.0164257 +Time = 0.00023 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 35 new parcels + +Cloud: sprayCloud + Current number of parcels = 2605 + Current mass in system = 3.52148e-10 + Linear momentum = (1.51398e-11 -3.83394e-09 0) + |Linear momentum| = 3.83397e-09 + Linear kinetic energy = 2.21355e-08 + model1: + number of parcels added = 2605 + mass introduced = 3.53678e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.136, 516.702 + Mass transfer phase change = 1.52976e-12 + D10, D32, Dmax (mu) = 38.9288, 78.9609, 148.614 + Liquid penetration 95% mass (m) = 0.00176972 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0131076, Final residual = 1.893e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0206312, Final residual = 4.85819e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00741078, Final residual = 6.4488e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00754431, Final residual = 4.11267e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00794418, Final residual = 2.5323e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00794419, Final residual = 2.53598e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00750566, Final residual = 4.91898e-07, No Iterations 1 +min/max(T) = 621.524, 811.283 +GAMG: Solving for p, Initial residual = 0.0490993, Final residual = 0.000562023, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.26983e-07, global = 4.88892e-07, cumulative = 3.54429e-05 +GAMG: Solving for p, Initial residual = 0.000573934, Final residual = 1.95821e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.81073e-07, global = 4.81057e-07, cumulative = 3.5924e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000446465, Final residual = 3.2706e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00809731, Final residual = 8.43472e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.076129 s +other Time = 1e-06 s +rho Equations = 0.000139 s +U Equations = 0.001078 s +Y Equations = 0.00232234 s +E Equations = 0.000587 s +p Equations = 0.001902 s +calculate parcels = 2.08153 s +chemistry correctThermo = 0.00197 s +turbulence correct = 0.000904 s +combustion correct(in Y) = 0.0670617 s +percentage of chemistry = 88.0895 % +percentage of rho/U/Y/E = 5.4202 % +========Time details of each equation======= +rhoEqn Time = 0.000254 s +rhoEqn assamble = 0.000201 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001077 s +UEqn assamble = 0.00065 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000427 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001734 s +YEqn assamble = 0.000631 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000221 s +YEqn correct boundary = 0 s +EEqn Time = 0.000458 s +EEqn assamble = 0.000343 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 9.8 s ClockTime = 10 s +Courant Number mean: 0.000226239 max: 0.0164445 +Time = 0.0002325 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 47 new parcels + +Cloud: sprayCloud + Current number of parcels = 2652 + Current mass in system = 3.56773e-10 + Linear momentum = (1.72852e-11 -3.88066e-09 0) + |Linear momentum| = 3.8807e-09 + Linear kinetic energy = 2.2375e-08 + model1: + number of parcels added = 2652 + mass introduced = 3.58346e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.135, 516.567 + Mass transfer phase change = 1.57249e-12 + D10, D32, Dmax (mu) = 39.1143, 78.9888, 148.618 + Liquid penetration 95% mass (m) = 0.0017944 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0115858, Final residual = 1.65449e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0202547, Final residual = 4.8023e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00730957, Final residual = 6.31005e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00750484, Final residual = 3.99299e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00787389, Final residual = 2.52915e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00787391, Final residual = 2.5327e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00744735, Final residual = 4.82722e-07, No Iterations 1 +min/max(T) = 620.766, 811.489 +GAMG: Solving for p, Initial residual = 0.0519897, Final residual = 0.000576736, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.36752e-07, global = 5.00235e-07, cumulative = 3.64242e-05 +GAMG: Solving for p, Initial residual = 0.000590405, Final residual = 8.46009e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.92631e-07, global = 4.92569e-07, cumulative = 3.69168e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000452908, Final residual = 3.3762e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00806997, Final residual = 8.49406e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.088969 s +other Time = 0 s +rho Equations = 0.000142 s +U Equations = 0.001029 s +Y Equations = 0.0024949 s +E Equations = 0.000603 s +p Equations = 0.002211 s +calculate parcels = 2.12212 s +chemistry correctThermo = 0.002801 s +turbulence correct = 0.001 s +combustion correct(in Y) = 0.0785181 s +percentage of chemistry = 88.2533 % +percentage of rho/U/Y/E = 4.79819 % +========Time details of each equation======= +rhoEqn Time = 0.000282 s +rhoEqn assamble = 0.000222 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001029 s +UEqn assamble = 0.00058 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000449 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001759 s +YEqn assamble = 0.000664 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000141 s +YEqn correct boundary = 0 s +EEqn Time = 0.000449 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 9.93 s ClockTime = 10 s +Courant Number mean: 0.000229339 max: 0.0164865 +Time = 0.000235 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 58 new parcels + +Cloud: sprayCloud + Current number of parcels = 2710 + Current mass in system = 3.62466e-10 + Linear momentum = (1.69449e-11 -3.94103e-09 0) + |Linear momentum| = 3.94106e-09 + Linear kinetic energy = 2.27031e-08 + model1: + number of parcels added = 2710 + mass introduced = 3.64082e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.136, 516.422 + Mass transfer phase change = 1.61633e-12 + D10, D32, Dmax (mu) = 39.2667, 78.9124, 148.622 + Liquid penetration 95% mass (m) = 0.00181926 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0103645, Final residual = 1.49927e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0197921, Final residual = 4.6953e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00715657, Final residual = 6.09943e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00746858, Final residual = 3.84358e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00779946, Final residual = 2.52684e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00779947, Final residual = 2.53035e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00733886, Final residual = 4.64773e-07, No Iterations 1 +min/max(T) = 620.135, 811.693 +GAMG: Solving for p, Initial residual = 0.0571969, Final residual = 0.000849897, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.5928e-07, global = 5.15758e-07, cumulative = 3.74325e-05 +GAMG: Solving for p, Initial residual = 0.000882033, Final residual = 2.56312e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.0529e-07, global = 5.05274e-07, cumulative = 3.79378e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.00045904, Final residual = 3.48206e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00803851, Final residual = 8.54821e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.090947 s +other Time = 0 s +rho Equations = 0.000133 s +U Equations = 0.00102 s +Y Equations = 0.00242172 s +E Equations = 0.000631 s +p Equations = 0.002043 s +calculate parcels = 2.16555 s +chemistry correctThermo = 0.002501 s +turbulence correct = 0.000852 s +combustion correct(in Y) = 0.0811693 s +percentage of chemistry = 89.249 % +percentage of rho/U/Y/E = 4.62436 % +========Time details of each equation======= +rhoEqn Time = 0.000256 s +rhoEqn assamble = 0.000198 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00102 s +UEqn assamble = 0.000594 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000426 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001608 s +YEqn assamble = 0.000631 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000477 s +EEqn assamble = 0.000361 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 10.06 s ClockTime = 10 s +Courant Number mean: 0.000232312 max: 0.0165652 +Time = 0.0002375 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 47 new parcels + +Cloud: sprayCloud + Current number of parcels = 2757 + Current mass in system = 3.67076e-10 + Linear momentum = (1.81003e-11 -3.98707e-09 0) + |Linear momentum| = 3.98711e-09 + Linear kinetic energy = 2.29358e-08 + model1: + number of parcels added = 2757 + mass introduced = 3.68737e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.132, 516.267 + Mass transfer phase change = 1.66109e-12 + D10, D32, Dmax (mu) = 39.4555, 78.8689, 148.626 + Liquid penetration 95% mass (m) = 0.00184304 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00999486, Final residual = 9.7839e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0192796, Final residual = 4.5487e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00703288, Final residual = 5.94965e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00741511, Final residual = 3.7475e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00773384, Final residual = 2.52392e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00773385, Final residual = 2.52734e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00728302, Final residual = 4.61396e-07, No Iterations 1 +min/max(T) = 619.599, 811.893 +GAMG: Solving for p, Initial residual = 0.0611962, Final residual = 0.000730833, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.5991e-07, global = 5.23004e-07, cumulative = 3.84608e-05 +GAMG: Solving for p, Initial residual = 0.000761595, Final residual = 6.84833e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.15909e-07, global = 5.15868e-07, cumulative = 3.89767e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.00046552, Final residual = 3.59332e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00800943, Final residual = 8.60454e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.090356 s +other Time = 0 s +rho Equations = 0.000143 s +U Equations = 0.000967 s +Y Equations = 0.00232719 s +E Equations = 0.000603 s +p Equations = 0.002184 s +calculate parcels = 2.21394 s +chemistry correctThermo = 0.002764 s +turbulence correct = 0.001062 s +combustion correct(in Y) = 0.0801348 s +percentage of chemistry = 88.6879 % +percentage of rho/U/Y/E = 4.47141 % +========Time details of each equation======= +rhoEqn Time = 0.000282 s +rhoEqn assamble = 0.000226 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000966 s +UEqn assamble = 0.000599 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000367 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001769 s +YEqn assamble = 0.000659 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00023 s +YEqn correct boundary = 0 s +EEqn Time = 0.000446 s +EEqn assamble = 0.000333 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 10.2 s ClockTime = 11 s +Courant Number mean: 0.00023506 max: 0.0165925 +Time = 0.00024 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 2803 + Current mass in system = 3.71567e-10 + Linear momentum = (1.72019e-11 -4.03139e-09 0) + |Linear momentum| = 4.03142e-09 + Linear kinetic energy = 2.31557e-08 + model1: + number of parcels added = 2803 + mass introduced = 3.73273e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.148, 516.105 + Mass transfer phase change = 1.70684e-12 + D10, D32, Dmax (mu) = 39.6251, 78.7502, 148.63 + Liquid penetration 95% mass (m) = 0.00186633 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00929077, Final residual = 9.32013e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0187104, Final residual = 4.4218e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00699458, Final residual = 5.79641e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00735892, Final residual = 3.65797e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0076548, Final residual = 2.51906e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00765481, Final residual = 2.52243e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00719766, Final residual = 4.57876e-07, No Iterations 1 +min/max(T) = 619.142, 812.094 +GAMG: Solving for p, Initial residual = 0.0661524, Final residual = 0.000622047, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.6373e-07, global = 5.33817e-07, cumulative = 3.95105e-05 +GAMG: Solving for p, Initial residual = 0.000649961, Final residual = 6.36317e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.27339e-07, global = 5.27302e-07, cumulative = 4.00378e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000472114, Final residual = 3.70767e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00798005, Final residual = 8.65956e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.10089 s +other Time = 0 s +rho Equations = 0.000148 s +U Equations = 0.001163 s +Y Equations = 0.00239228 s +E Equations = 0.000619 s +p Equations = 0.002143 s +calculate parcels = 2.26487 s +chemistry correctThermo = 0.002779 s +turbulence correct = 0.001016 s +combustion correct(in Y) = 0.0904487 s +percentage of chemistry = 89.6508 % +percentage of rho/U/Y/E = 4.28415 % +========Time details of each equation======= +rhoEqn Time = 0.000286 s +rhoEqn assamble = 0.000226 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001161 s +UEqn assamble = 0.000718 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000443 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001744 s +YEqn assamble = 0.000653 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000197 s +YEqn correct boundary = 0 s +EEqn Time = 0.000461 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000125 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 10.36 s ClockTime = 11 s +Courant Number mean: 0.000237618 max: 0.0166284 +Time = 0.0002425 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 58 new parcels + +Cloud: sprayCloud + Current number of parcels = 2861 + Current mass in system = 3.77214e-10 + Linear momentum = (1.79478e-11 -4.09039e-09 0) + |Linear momentum| = 4.09043e-09 + Linear kinetic energy = 2.34707e-08 + model1: + number of parcels added = 2861 + mass introduced = 3.78967e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.132, 515.936 + Mass transfer phase change = 1.75357e-12 + D10, D32, Dmax (mu) = 39.8056, 78.7107, 148.633 + Liquid penetration 95% mass (m) = 0.00189027 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00963996, Final residual = 1.48003e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0180264, Final residual = 4.27057e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00695452, Final residual = 5.65483e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0073024, Final residual = 3.59056e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00758336, Final residual = 2.51532e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00758337, Final residual = 2.51867e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00713533, Final residual = 4.52039e-07, No Iterations 1 +min/max(T) = 618.764, 812.295 +GAMG: Solving for p, Initial residual = 0.0737304, Final residual = 0.000683907, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.73742e-07, global = 5.44838e-07, cumulative = 4.05826e-05 +GAMG: Solving for p, Initial residual = 0.000722118, Final residual = 9.45164e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.38719e-07, global = 5.38673e-07, cumulative = 4.11213e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000478649, Final residual = 3.82925e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00794921, Final residual = 8.71777e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.088809 s +other Time = 1e-06 s +rho Equations = 0.000166 s +U Equations = 0.001241 s +Y Equations = 0.00207017 s +E Equations = 0.000491 s +p Equations = 0.002541 s +calculate parcels = 2.32527 s +chemistry correctThermo = 0.003018 s +turbulence correct = 0.001135 s +combustion correct(in Y) = 0.0779288 s +percentage of chemistry = 87.7488 % +percentage of rho/U/Y/E = 4.4682 % +========Time details of each equation======= +rhoEqn Time = 0.00035 s +rhoEqn assamble = 0.000262 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00124 s +UEqn assamble = 0.000737 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000503 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001421 s +YEqn assamble = 0.000541 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.2e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000372 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 10.51 s ClockTime = 11 s +Courant Number mean: 0.000240078 max: 0.0166719 +Time = 0.000245 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 39 new parcels + +Cloud: sprayCloud + Current number of parcels = 2900 + Current mass in system = 3.80999e-10 + Linear momentum = (1.97908e-11 -4.12512e-09 0) + |Linear momentum| = 4.12517e-09 + Linear kinetic energy = 2.3626e-08 + model1: + number of parcels added = 2900 + mass introduced = 3.828e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.151, 515.762 + Mass transfer phase change = 1.80115e-12 + D10, D32, Dmax (mu) = 39.7764, 78.5848, 148.637 + Liquid penetration 95% mass (m) = 0.00191634 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.01046, Final residual = 1.64217e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0172682, Final residual = 4.09867e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00688881, Final residual = 5.52357e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00723224, Final residual = 3.56007e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00750841, Final residual = 2.50628e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00750842, Final residual = 2.50959e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0070449, Final residual = 4.43763e-07, No Iterations 1 +min/max(T) = 618.455, 812.493 +GAMG: Solving for p, Initial residual = 0.082711, Final residual = 0.000778078, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.85103e-07, global = 5.53793e-07, cumulative = 4.16751e-05 +GAMG: Solving for p, Initial residual = 0.000829267, Final residual = 2.62942e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.48467e-07, global = 5.48455e-07, cumulative = 4.22236e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000485123, Final residual = 3.95942e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00791767, Final residual = 8.78079e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.0816 s +other Time = 0 s +rho Equations = 0.000162 s +U Equations = 0.001243 s +Y Equations = 0.00224602 s +E Equations = 0.000503 s +p Equations = 0.002048 s +calculate parcels = 2.38685 s +chemistry correctThermo = 0.002018 s +turbulence correct = 0.000839 s +combustion correct(in Y) = 0.072353 s +percentage of chemistry = 88.6679 % +percentage of rho/U/Y/E = 5.09071 % +========Time details of each equation======= +rhoEqn Time = 0.000288 s +rhoEqn assamble = 0.000228 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00124 s +UEqn assamble = 0.000719 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000521 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001582 s +YEqn assamble = 0.000577 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00017 s +YEqn correct boundary = 0 s +EEqn Time = 0.000375 s +EEqn assamble = 0.00028 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 10.65 s ClockTime = 11 s +Courant Number mean: 0.000242507 max: 0.0167049 +Time = 0.0002475 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 37 new parcels + +Cloud: sprayCloud + Current number of parcels = 2937 + Current mass in system = 3.84558e-10 + Linear momentum = (1.94854e-11 -4.15669e-09 0) + |Linear momentum| = 4.15674e-09 + Linear kinetic energy = 2.37604e-08 + model1: + number of parcels added = 2937 + mass introduced = 3.86408e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.136, 515.583 + Mass transfer phase change = 1.84955e-12 + D10, D32, Dmax (mu) = 39.882, 78.5193, 148.64 + Liquid penetration 95% mass (m) = 0.00194062 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0108343, Final residual = 1.81589e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0164294, Final residual = 3.92003e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00681925, Final residual = 5.35359e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00716081, Final residual = 3.52565e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00743442, Final residual = 2.49969e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00743443, Final residual = 2.50295e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00694389, Final residual = 4.35564e-07, No Iterations 1 +min/max(T) = 618.202, 812.691 +GAMG: Solving for p, Initial residual = 0.0921983, Final residual = 0.000781248, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.91782e-07, global = 5.63554e-07, cumulative = 4.27871e-05 +GAMG: Solving for p, Initial residual = 0.000803215, Final residual = 1.85434e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.57813e-07, global = 5.57805e-07, cumulative = 4.33449e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000491654, Final residual = 4.09267e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00788562, Final residual = 8.84244e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.066865 s +other Time = 1e-06 s +rho Equations = 0.000146 s +U Equations = 0.001053 s +Y Equations = 0.00212843 s +E Equations = 0.000507 s +p Equations = 0.00202 s +calculate parcels = 2.43141 s +chemistry correctThermo = 0.001969 s +turbulence correct = 0.000838 s +combustion correct(in Y) = 0.0579836 s +percentage of chemistry = 86.7174 % +percentage of rho/U/Y/E = 5.73458 % +========Time details of each equation======= +rhoEqn Time = 0.00027 s +rhoEqn assamble = 0.000213 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001052 s +UEqn assamble = 0.000641 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000411 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00156 s +YEqn assamble = 0.000583 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000137 s +YEqn correct boundary = 0 s +EEqn Time = 0.000379 s +EEqn assamble = 0.000288 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 10.76 s ClockTime = 11 s +Courant Number mean: 0.000244885 max: 0.0167336 +Time = 0.00025 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 40 new parcels + +Cloud: sprayCloud + Current number of parcels = 2977 + Current mass in system = 3.88374e-10 + Linear momentum = (1.94201e-11 -4.19136e-09 0) + |Linear momentum| = 4.19141e-09 + Linear kinetic energy = 2.39129e-08 + model1: + number of parcels added = 2977 + mass introduced = 3.90273e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.132, 515.392 + Mass transfer phase change = 1.89886e-12 + D10, D32, Dmax (mu) = 39.6361, 78.2579, 148.644 + Liquid penetration 95% mass (m) = 0.00196543 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0112536, Final residual = 1.93946e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0155593, Final residual = 3.73894e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00676266, Final residual = 5.35385e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00709813, Final residual = 3.5106e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00736576, Final residual = 2.48847e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00736578, Final residual = 2.49167e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00687217, Final residual = 4.23846e-07, No Iterations 1 +min/max(T) = 617.967, 812.888 +GAMG: Solving for p, Initial residual = 0.10133, Final residual = 0.00102295, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.06118e-07, global = 5.76266e-07, cumulative = 4.39212e-05 +GAMG: Solving for p, Initial residual = 0.00103031, Final residual = 2.96744e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.68306e-07, global = 5.68294e-07, cumulative = 4.44895e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000497998, Final residual = 4.22617e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00785176, Final residual = 8.8992e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.073116 s +other Time = 0 s +rho Equations = 0.000148 s +U Equations = 0.001245 s +Y Equations = 0.00239087 s +E Equations = 0.000504 s +p Equations = 0.002144 s +calculate parcels = 2.47606 s +chemistry correctThermo = 0.001909 s +turbulence correct = 0.000862 s +combustion correct(in Y) = 0.0637431 s +percentage of chemistry = 87.1808 % +percentage of rho/U/Y/E = 5.86447 % +========Time details of each equation======= +rhoEqn Time = 0.000281 s +rhoEqn assamble = 0.000225 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001243 s +UEqn assamble = 0.000821 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000422 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00182 s +YEqn assamble = 0.000734 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000167 s +YEqn correct boundary = 0 s +EEqn Time = 0.000376 s +EEqn assamble = 0.000282 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 10.88 s ClockTime = 11 s +Courant Number mean: 0.000247223 max: 0.0167954 +Time = 0.0002525 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 39 new parcels + +Cloud: sprayCloud + Current number of parcels = 3016 + Current mass in system = 3.92063e-10 + Linear momentum = (1.88106e-11 -4.22422e-09 0) + |Linear momentum| = 4.22426e-09 + Linear kinetic energy = 2.4053e-08 + model1: + number of parcels added = 3016 + mass introduced = 3.94012e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.126, 515.179 + Mass transfer phase change = 1.94885e-12 + D10, D32, Dmax (mu) = 39.7587, 78.171, 149.255 + Liquid penetration 95% mass (m) = 0.00199081 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0121531, Final residual = 2.02839e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.014697, Final residual = 3.52625e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00666356, Final residual = 5.28993e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00701326, Final residual = 3.47018e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00729197, Final residual = 2.47671e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00729198, Final residual = 2.47986e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00675248, Final residual = 4.226e-07, No Iterations 1 +min/max(T) = 617.771, 813.083 +GAMG: Solving for p, Initial residual = 0.108858, Final residual = 0.0011038, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.16674e-07, global = 5.83632e-07, cumulative = 4.50731e-05 +GAMG: Solving for p, Initial residual = 0.00106695, Final residual = 2.45137e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.76281e-07, global = 5.76272e-07, cumulative = 4.56494e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000504903, Final residual = 4.3715e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00782181, Final residual = 8.96479e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103682 s +other Time = 0 s +rho Equations = 0.000145 s +U Equations = 0.001059 s +Y Equations = 0.00235281 s +E Equations = 0.000606 s +p Equations = 0.002391 s +calculate parcels = 2.52097 s +chemistry correctThermo = 0.002769 s +turbulence correct = 0.000958 s +combustion correct(in Y) = 0.0932242 s +percentage of chemistry = 89.9136 % +percentage of rho/U/Y/E = 4.01498 % +========Time details of each equation======= +rhoEqn Time = 0.000288 s +rhoEqn assamble = 0.000226 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001058 s +UEqn assamble = 0.000642 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000416 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001771 s +YEqn assamble = 0.000652 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000212 s +YEqn correct boundary = 0 s +EEqn Time = 0.000452 s +EEqn assamble = 0.000339 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 11.03 s ClockTime = 11 s +Courant Number mean: 0.000249437 max: 0.0168025 +Time = 0.000255 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 36 new parcels + +Cloud: sprayCloud + Current number of parcels = 3052 + Current mass in system = 3.95434e-10 + Linear momentum = (1.90082e-11 -4.2528e-09 0) + |Linear momentum| = 4.25285e-09 + Linear kinetic energy = 2.4165e-08 + model1: + number of parcels added = 3052 + mass introduced = 3.97434e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.127, 514.937 + Mass transfer phase change = 1.99947e-12 + D10, D32, Dmax (mu) = 39.88, 78.1538, 148.695 + Liquid penetration 95% mass (m) = 0.00201756 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0111771, Final residual = 1.92244e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0138733, Final residual = 3.3757e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00656308, Final residual = 5.2399e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00693353, Final residual = 3.41878e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00722899, Final residual = 2.46586e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.007229, Final residual = 2.46897e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00662228, Final residual = 4.21382e-07, No Iterations 1 +min/max(T) = 617.615, 813.281 +GAMG: Solving for p, Initial residual = 0.113904, Final residual = 0.00141481, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.3515e-07, global = 5.96094e-07, cumulative = 4.62455e-05 +GAMG: Solving for p, Initial residual = 0.00133369, Final residual = 3.68736e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.83448e-07, global = 5.83434e-07, cumulative = 4.68289e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000512288, Final residual = 4.53298e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00779494, Final residual = 9.04332e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.083243 s +other Time = 0 s +rho Equations = 0.000159 s +U Equations = 0.001231 s +Y Equations = 0.00203527 s +E Equations = 0.000496 s +p Equations = 0.001927 s +calculate parcels = 2.57529 s +chemistry correctThermo = 0.001955 s +turbulence correct = 0.000814 s +combustion correct(in Y) = 0.0744427 s +percentage of chemistry = 89.4282 % +percentage of rho/U/Y/E = 4.71063 % +========Time details of each equation======= +rhoEqn Time = 0.000276 s +rhoEqn assamble = 0.000218 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00123 s +UEqn assamble = 0.000704 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000526 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001373 s +YEqn assamble = 0.000515 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.6e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000374 s +EEqn assamble = 0.000279 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 11.16 s ClockTime = 12 s +Courant Number mean: 0.000251489 max: 0.0167863 +Time = 0.0002575 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 40 new parcels + +Cloud: sprayCloud + Current number of parcels = 3092 + Current mass in system = 3.99147e-10 + Linear momentum = (1.99705e-11 -4.28557e-09 0) + |Linear momentum| = 4.28562e-09 + Linear kinetic energy = 2.43028e-08 + model1: + number of parcels added = 3092 + mass introduced = 4.01198e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.14, 514.668 + Mass transfer phase change = 2.0509e-12 + D10, D32, Dmax (mu) = 39.9149, 78.0733, 148.655 + Liquid penetration 95% mass (m) = 0.00204228 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00970054, Final residual = 1.80552e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0129905, Final residual = 3.2339e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00649734, Final residual = 5.24869e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00686682, Final residual = 3.3849e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00715995, Final residual = 2.46166e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00715996, Final residual = 2.46496e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00652969, Final residual = 4.11104e-07, No Iterations 1 +min/max(T) = 617.524, 813.483 +GAMG: Solving for p, Initial residual = 0.1152, Final residual = 0.00106723, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.30708e-07, global = 6.01511e-07, cumulative = 4.74304e-05 +GAMG: Solving for p, Initial residual = 0.00101039, Final residual = 1.43482e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.92776e-07, global = 5.92771e-07, cumulative = 4.80232e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000519328, Final residual = 4.69699e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00776548, Final residual = 9.11903e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.076239 s +other Time = 1e-06 s +rho Equations = 0.000238 s +U Equations = 0.001573 s +Y Equations = 0.00238826 s +E Equations = 0.000594 s +p Equations = 0.002371 s +calculate parcels = 2.63457 s +chemistry correctThermo = 0.002797 s +turbulence correct = 0.000991 s +combustion correct(in Y) = 0.0650027 s +percentage of chemistry = 85.2618 % +percentage of rho/U/Y/E = 6.28715 % +========Time details of each equation======= +rhoEqn Time = 0.000382 s +rhoEqn assamble = 0.000303 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001571 s +UEqn assamble = 0.000917 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000654 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001657 s +YEqn assamble = 0.000627 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000128 s +YEqn correct boundary = 0 s +EEqn Time = 0.000441 s +EEqn assamble = 0.000328 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 11.3 s ClockTime = 12 s +Courant Number mean: 0.000253425 max: 0.0168114 +Time = 0.00026 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 39 new parcels + +Cloud: sprayCloud + Current number of parcels = 3131 + Current mass in system = 4.02735e-10 + Linear momentum = (2.06062e-11 -4.31659e-09 0) + |Linear momentum| = 4.31664e-09 + Linear kinetic energy = 2.44287e-08 + model1: + number of parcels added = 3131 + mass introduced = 4.04838e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.134, 514.374 + Mass transfer phase change = 2.10305e-12 + D10, D32, Dmax (mu) = 40.0393, 78.0631, 148.659 + Liquid penetration 95% mass (m) = 0.00206719 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00881145, Final residual = 1.66563e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0121158, Final residual = 3.05879e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0064185, Final residual = 5.24525e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00679381, Final residual = 3.37309e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00709092, Final residual = 2.45817e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00709093, Final residual = 2.4615e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00641918, Final residual = 4.12327e-07, No Iterations 1 +min/max(T) = 617.462, 813.681 +GAMG: Solving for p, Initial residual = 0.118307, Final residual = 0.00116993, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.38612e-07, global = 6.09636e-07, cumulative = 4.86328e-05 +GAMG: Solving for p, Initial residual = 0.00111022, Final residual = 8.01991e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.01101e-07, global = 6.01073e-07, cumulative = 4.92339e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000526791, Final residual = 4.86726e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00773792, Final residual = 9.19552e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.08962 s +other Time = 0 s +rho Equations = 0.000158 s +U Equations = 0.001198 s +Y Equations = 0.00251519 s +E Equations = 0.000612 s +p Equations = 0.002294 s +calculate parcels = 2.69756 s +chemistry correctThermo = 0.002804 s +turbulence correct = 0.000983 s +combustion correct(in Y) = 0.0788628 s +percentage of chemistry = 87.9969 % +percentage of rho/U/Y/E = 5.00244 % +========Time details of each equation======= +rhoEqn Time = 0.000306 s +rhoEqn assamble = 0.000243 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001197 s +UEqn assamble = 0.000699 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000498 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001847 s +YEqn assamble = 0.000697 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000177 s +YEqn correct boundary = 0 s +EEqn Time = 0.000454 s +EEqn assamble = 0.000341 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 11.45 s ClockTime = 12 s +Courant Number mean: 0.000255129 max: 0.016797 +Time = 0.0002625 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 3181 + Current mass in system = 4.0731e-10 + Linear momentum = (2.18507e-11 -4.3598e-09 0) + |Linear momentum| = 4.35985e-09 + Linear kinetic energy = 2.46314e-08 + model1: + number of parcels added = 3181 + mass introduced = 4.09466e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.135, 514.059 + Mass transfer phase change = 2.15599e-12 + D10, D32, Dmax (mu) = 40.1202, 78.0058, 148.663 + Liquid penetration 95% mass (m) = 0.00209164 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00811525, Final residual = 1.59538e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0114845, Final residual = 2.96129e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00634818, Final residual = 5.266e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00672512, Final residual = 3.37483e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00702251, Final residual = 2.45837e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00702253, Final residual = 2.46167e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0063349, Final residual = 4.07427e-07, No Iterations 1 +min/max(T) = 617.449, 813.88 +GAMG: Solving for p, Initial residual = 0.117013, Final residual = 0.00114577, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.47888e-07, global = 6.18987e-07, cumulative = 4.98529e-05 +GAMG: Solving for p, Initial residual = 0.0011255, Final residual = 2.49145e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.10216e-07, global = 6.10208e-07, cumulative = 5.04631e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000533855, Final residual = 5.03961e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00770788, Final residual = 9.2688e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.083015 s +other Time = 0 s +rho Equations = 0.000134 s +U Equations = 0.001061 s +Y Equations = 0.00234815 s +E Equations = 0.000601 s +p Equations = 0.002395 s +calculate parcels = 2.75053 s +chemistry correctThermo = 0.002772 s +turbulence correct = 0.001004 s +combustion correct(in Y) = 0.0725299 s +percentage of chemistry = 87.3696 % +percentage of rho/U/Y/E = 4.99205 % +========Time details of each equation======= +rhoEqn Time = 0.000283 s +rhoEqn assamble = 0.000223 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00106 s +UEqn assamble = 0.00063 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00043 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001775 s +YEqn assamble = 0.000659 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000231 s +YEqn correct boundary = 0 s +EEqn Time = 0.000449 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 11.59 s ClockTime = 12 s +Courant Number mean: 0.000256691 max: 0.0168186 +Time = 0.000265 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 40 new parcels + +Cloud: sprayCloud + Current number of parcels = 3221 + Current mass in system = 4.10946e-10 + Linear momentum = (2.15948e-11 -4.39105e-09 0) + |Linear momentum| = 4.39111e-09 + Linear kinetic energy = 2.47564e-08 + model1: + number of parcels added = 3221 + mass introduced = 4.13156e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.129, 513.725 + Mass transfer phase change = 2.20954e-12 + D10, D32, Dmax (mu) = 40.2426, 77.8834, 148.989 + Liquid penetration 95% mass (m) = 0.00211561 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00829978, Final residual = 1.59719e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0119588, Final residual = 3.06582e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00625293, Final residual = 5.20978e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00664615, Final residual = 3.32949e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00695682, Final residual = 2.45721e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00695684, Final residual = 2.46048e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00622717, Final residual = 4.06233e-07, No Iterations 1 +min/max(T) = 617.44, 814.078 +GAMG: Solving for p, Initial residual = 0.11237, Final residual = 0.0011428, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.52506e-07, global = 6.23712e-07, cumulative = 5.10868e-05 +GAMG: Solving for p, Initial residual = 0.00109349, Final residual = 2.43128e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.17172e-07, global = 6.17163e-07, cumulative = 5.1704e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000541301, Final residual = 5.22292e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00767961, Final residual = 9.34768e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09252 s +other Time = 1e-06 s +rho Equations = 0.00017 s +U Equations = 0.001226 s +Y Equations = 0.00234721 s +E Equations = 0.000628 s +p Equations = 0.001986 s +calculate parcels = 2.80846 s +chemistry correctThermo = 0.002353 s +turbulence correct = 0.000821 s +combustion correct(in Y) = 0.0827928 s +percentage of chemistry = 89.4864 % +percentage of rho/U/Y/E = 4.72461 % +========Time details of each equation======= +rhoEqn Time = 0.000291 s +rhoEqn assamble = 0.000221 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001224 s +UEqn assamble = 0.0007 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000524 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001692 s +YEqn assamble = 0.000623 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000181 s +YEqn correct boundary = 0 s +EEqn Time = 0.000459 s +EEqn assamble = 0.000343 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 11.74 s ClockTime = 12 s +Courant Number mean: 0.000258072 max: 0.0168008 +Time = 0.0002675 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 47 new parcels + +Cloud: sprayCloud + Current number of parcels = 3268 + Current mass in system = 4.15193e-10 + Linear momentum = (2.13309e-11 -4.42967e-09 0) + |Linear momentum| = 4.42972e-09 + Linear kinetic energy = 2.49274e-08 + model1: + number of parcels added = 3268 + mass introduced = 4.17456e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.148, 513.373 + Mass transfer phase change = 2.26378e-12 + D10, D32, Dmax (mu) = 38.9956, 77.7503, 148.671 + Liquid penetration 95% mass (m) = 0.00213889 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00895532, Final residual = 1.83205e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0127546, Final residual = 3.26702e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00617255, Final residual = 5.21376e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00657386, Final residual = 3.32735e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00689072, Final residual = 2.47205e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00689074, Final residual = 2.47543e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00614489, Final residual = 4.02139e-07, No Iterations 1 +min/max(T) = 617.483, 814.279 +GAMG: Solving for p, Initial residual = 0.101161, Final residual = 0.00100634, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.63211e-07, global = 6.35648e-07, cumulative = 5.23396e-05 +GAMG: Solving for p, Initial residual = 0.000950512, Final residual = 1.64812e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.25176e-07, global = 6.25169e-07, cumulative = 5.29648e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.00054827, Final residual = 5.40415e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00764866, Final residual = 9.42032e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.079277 s +other Time = 1e-06 s +rho Equations = 0.000138 s +U Equations = 0.001065 s +Y Equations = 0.00207398 s +E Equations = 0.000661 s +p Equations = 0.002408 s +calculate parcels = 2.86354 s +chemistry correctThermo = 0.002793 s +turbulence correct = 0.001011 s +combustion correct(in Y) = 0.068955 s +percentage of chemistry = 86.9799 % +percentage of rho/U/Y/E = 4.96737 % +========Time details of each equation======= +rhoEqn Time = 0.000281 s +rhoEqn assamble = 0.000221 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001064 s +UEqn assamble = 0.00063 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000434 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00151 s +YEqn assamble = 0.000558 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00014 s +YEqn correct boundary = 0 s +EEqn Time = 0.00054 s +EEqn assamble = 0.000407 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000133 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 11.87 s ClockTime = 12 s +Courant Number mean: 0.000259343 max: 0.0168316 +Time = 0.00027 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 3314 + Current mass in system = 4.19327e-10 + Linear momentum = (2.1755e-11 -4.46655e-09 0) + |Linear momentum| = 4.4666e-09 + Linear kinetic energy = 2.50867e-08 + model1: + number of parcels added = 3314 + mass introduced = 4.21645e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.134, 513.006 + Mass transfer phase change = 2.31866e-12 + D10, D32, Dmax (mu) = 39.1176, 77.6678, 148.675 + Liquid penetration 95% mass (m) = 0.00216362 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0096745, Final residual = 1.93265e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0135539, Final residual = 3.42259e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00608595, Final residual = 5.18385e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00649429, Final residual = 3.31515e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00681641, Final residual = 2.47921e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00681643, Final residual = 2.48256e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00605737, Final residual = 4.06869e-07, No Iterations 1 +min/max(T) = 617.586, 814.477 +GAMG: Solving for p, Initial residual = 0.0907143, Final residual = 0.000789038, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.64599e-07, global = 6.4142e-07, cumulative = 5.36062e-05 +GAMG: Solving for p, Initial residual = 0.000748573, Final residual = 5.32089e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.32621e-07, global = 6.326e-07, cumulative = 5.42388e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000555312, Final residual = 5.59112e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0076181, Final residual = 9.49339e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.089089 s +other Time = 1e-06 s +rho Equations = 0.000138 s +U Equations = 0.001036 s +Y Equations = 0.00230365 s +E Equations = 0.000597 s +p Equations = 0.002505 s +calculate parcels = 2.92829 s +chemistry correctThermo = 0.002737 s +turbulence correct = 0.001167 s +combustion correct(in Y) = 0.0784283 s +percentage of chemistry = 88.0337 % +percentage of rho/U/Y/E = 4.57369 % +========Time details of each equation======= +rhoEqn Time = 0.000322 s +rhoEqn assamble = 0.000257 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001036 s +UEqn assamble = 0.000595 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000441 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001718 s +YEqn assamble = 0.000617 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000219 s +YEqn correct boundary = 0 s +EEqn Time = 0.000444 s +EEqn assamble = 0.000331 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 12.03 s ClockTime = 12 s +Courant Number mean: 0.000260489 max: 0.0168365 +Time = 0.0002725 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 54 new parcels + +Cloud: sprayCloud + Current number of parcels = 3368 + Current mass in system = 4.24163e-10 + Linear momentum = (2.1403e-11 -4.51197e-09 0) + |Linear momentum| = 4.51202e-09 + Linear kinetic energy = 2.52989e-08 + model1: + number of parcels added = 3368 + mass introduced = 4.26537e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.143, 513.924 + Mass transfer phase change = 2.37409e-12 + D10, D32, Dmax (mu) = 39.2429, 77.7437, 148.679 + Liquid penetration 95% mass (m) = 0.00218719 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00999906, Final residual = 1.94453e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0142516, Final residual = 3.58666e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.005992, Final residual = 5.15477e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00641294, Final residual = 3.30386e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00674534, Final residual = 2.48465e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00674537, Final residual = 2.48797e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00595489, Final residual = 4.1031e-07, No Iterations 1 +min/max(T) = 617.734, 814.677 +GAMG: Solving for p, Initial residual = 0.0847449, Final residual = 0.00089739, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.78988e-07, global = 6.47694e-07, cumulative = 5.48865e-05 +GAMG: Solving for p, Initial residual = 0.000857317, Final residual = 9.11717e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.38855e-07, global = 6.38811e-07, cumulative = 5.55253e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000562866, Final residual = 5.78798e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00759049, Final residual = 9.57011e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.086089 s +other Time = 1e-06 s +rho Equations = 0.000182 s +U Equations = 0.001218 s +Y Equations = 0.00216793 s +E Equations = 0.000493 s +p Equations = 0.002013 s +calculate parcels = 2.98636 s +chemistry correctThermo = 0.001995 s +turbulence correct = 0.000933 s +combustion correct(in Y) = 0.0768531 s +percentage of chemistry = 89.2716 % +percentage of rho/U/Y/E = 4.71713 % +========Time details of each equation======= +rhoEqn Time = 0.000307 s +rhoEqn assamble = 0.000242 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001217 s +UEqn assamble = 0.00071 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000507 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001488 s +YEqn assamble = 0.000576 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000372 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 12.17 s ClockTime = 13 s +Courant Number mean: 0.000261459 max: 0.0168111 +Time = 0.000275 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 39 new parcels + +Cloud: sprayCloud + Current number of parcels = 3407 + Current mass in system = 4.27635e-10 + Linear momentum = (2.13088e-11 -4.54021e-09 0) + |Linear momentum| = 4.54026e-09 + Linear kinetic energy = 2.5402e-08 + model1: + number of parcels added = 3407 + mass introduced = 4.30065e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.132, 515.495 + Mass transfer phase change = 2.43e-12 + D10, D32, Dmax (mu) = 39.3179, 77.6444, 148.683 + Liquid penetration 95% mass (m) = 0.00221141 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00983664, Final residual = 1.90719e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0147834, Final residual = 3.75319e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00589479, Final residual = 5.10718e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00633062, Final residual = 3.26364e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00667504, Final residual = 2.48958e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00667506, Final residual = 2.49283e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00584779, Final residual = 4.06231e-07, No Iterations 1 +min/max(T) = 617.875, 814.881 +GAMG: Solving for p, Initial residual = 0.0803156, Final residual = 0.000908771, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.87034e-07, global = 6.51543e-07, cumulative = 5.61768e-05 +GAMG: Solving for p, Initial residual = 0.000874462, Final residual = 9.58585e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.44519e-07, global = 6.4447e-07, cumulative = 5.68213e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.00057044, Final residual = 5.9936e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00756264, Final residual = 9.65035e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.085527 s +other Time = 0 s +rho Equations = 0.000172 s +U Equations = 0.001201 s +Y Equations = 0.00256427 s +E Equations = 0.000476 s +p Equations = 0.002228 s +calculate parcels = 3.0704 s +chemistry correctThermo = 0.001956 s +turbulence correct = 0.000968 s +combustion correct(in Y) = 0.0757677 s +percentage of chemistry = 88.5893 % +percentage of rho/U/Y/E = 5.16009 % +========Time details of each equation======= +rhoEqn Time = 0.000314 s +rhoEqn assamble = 0.000248 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.0012 s +UEqn assamble = 0.000704 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000496 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001931 s +YEqn assamble = 0.000768 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000239 s +YEqn correct boundary = 0 s +EEqn Time = 0.00036 s +EEqn assamble = 0.000268 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 12.34 s ClockTime = 13 s +Courant Number mean: 0.000262329 max: 0.0167939 +Time = 0.0002775 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 3458 + Current mass in system = 4.32152e-10 + Linear momentum = (2.15445e-11 -4.58123e-09 0) + |Linear momentum| = 4.58128e-09 + Linear kinetic energy = 2.55841e-08 + model1: + number of parcels added = 3458 + mass introduced = 4.34639e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.124, 516.832 + Mass transfer phase change = 2.48642e-12 + D10, D32, Dmax (mu) = 39.4413, 77.6089, 148.687 + Liquid penetration 95% mass (m) = 0.002235 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00998124, Final residual = 2.01348e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0151962, Final residual = 3.8703e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00580091, Final residual = 5.07214e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00625105, Final residual = 3.23768e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00660692, Final residual = 2.50652e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00660694, Final residual = 2.50994e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00575075, Final residual = 4.04795e-07, No Iterations 1 +min/max(T) = 618.007, 815.087 +GAMG: Solving for p, Initial residual = 0.0755342, Final residual = 0.000693369, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.85072e-07, global = 6.57167e-07, cumulative = 5.74785e-05 +GAMG: Solving for p, Initial residual = 0.000667012, Final residual = 9.06378e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.50376e-07, global = 6.50327e-07, cumulative = 5.81288e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000578047, Final residual = 6.20416e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00753489, Final residual = 9.73026e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09406 s +other Time = 1e-06 s +rho Equations = 0.000183 s +U Equations = 0.001174 s +Y Equations = 0.00239437 s +E Equations = 0.000605 s +p Equations = 0.002141 s +calculate parcels = 3.13905 s +chemistry correctThermo = 0.00281 s +turbulence correct = 0.001015 s +combustion correct(in Y) = 0.0835446 s +percentage of chemistry = 88.8206 % +percentage of rho/U/Y/E = 4.63148 % +========Time details of each equation======= +rhoEqn Time = 0.000319 s +rhoEqn assamble = 0.000249 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001174 s +UEqn assamble = 0.000679 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000495 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001756 s +YEqn assamble = 0.000668 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000184 s +YEqn correct boundary = 0 s +EEqn Time = 0.000443 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 12.5 s ClockTime = 13 s +Courant Number mean: 0.000263061 max: 0.0167863 +Time = 0.00028 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 52 new parcels + +Cloud: sprayCloud + Current number of parcels = 3510 + Current mass in system = 4.36745e-10 + Linear momentum = (2.15254e-11 -4.6229e-09 0) + |Linear momentum| = 4.62295e-09 + Linear kinetic energy = 2.57691e-08 + model1: + number of parcels added = 3510 + mass introduced = 4.39288e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.124, 517.951 + Mass transfer phase change = 2.54336e-12 + D10, D32, Dmax (mu) = 39.4586, 77.5622, 148.692 + Liquid penetration 95% mass (m) = 0.00225739 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00991606, Final residual = 2.03439e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0154788, Final residual = 3.9496e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00570897, Final residual = 5.02243e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00617378, Final residual = 3.2088e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00654141, Final residual = 2.52179e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00654143, Final residual = 2.5252e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00566693, Final residual = 4.06021e-07, No Iterations 1 +min/max(T) = 618.148, 815.293 +GAMG: Solving for p, Initial residual = 0.071978, Final residual = 0.000587734, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.8699e-07, global = 6.62739e-07, cumulative = 5.87915e-05 +GAMG: Solving for p, Initial residual = 0.000566234, Final residual = 8.23836e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.56247e-07, global = 6.56204e-07, cumulative = 5.94478e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.00058567, Final residual = 6.41956e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0075071, Final residual = 9.80975e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.083447 s +other Time = 0 s +rho Equations = 0.000132 s +U Equations = 0.001048 s +Y Equations = 0.00203613 s +E Equations = 0.000483 s +p Equations = 0.001815 s +calculate parcels = 3.20857 s +chemistry correctThermo = 0.001955 s +turbulence correct = 0.000821 s +combustion correct(in Y) = 0.0749969 s +percentage of chemistry = 89.8737 % +percentage of rho/U/Y/E = 4.43291 % +========Time details of each equation======= +rhoEqn Time = 0.000249 s +rhoEqn assamble = 0.000197 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001047 s +UEqn assamble = 0.000576 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000471 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001477 s +YEqn assamble = 0.000559 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000131 s +YEqn correct boundary = 0 s +EEqn Time = 0.000364 s +EEqn assamble = 0.000272 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 12.66 s ClockTime = 13 s +Courant Number mean: 0.000263659 max: 0.0167856 +Time = 0.0002825 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 3554 + Current mass in system = 4.40612e-10 + Linear momentum = (2.0955e-11 -4.65544e-09 0) + |Linear momentum| = 4.65549e-09 + Linear kinetic energy = 2.58969e-08 + model1: + number of parcels added = 3554 + mass introduced = 4.43213e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.148, 518.869 + Mass transfer phase change = 2.60059e-12 + D10, D32, Dmax (mu) = 39.5649, 77.5905, 149.331 + Liquid penetration 95% mass (m) = 0.00228119 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00974585, Final residual = 2.01457e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0156826, Final residual = 3.98606e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00559667, Final residual = 4.93445e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00608623, Final residual = 3.15587e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00647347, Final residual = 2.53457e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00647349, Final residual = 2.53797e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00555692, Final residual = 4.02717e-07, No Iterations 1 +min/max(T) = 618.306, 815.501 +GAMG: Solving for p, Initial residual = 0.0710948, Final residual = 0.000693508, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.9772e-07, global = 6.6705e-07, cumulative = 6.01148e-05 +GAMG: Solving for p, Initial residual = 0.000681495, Final residual = 9.31257e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.59721e-07, global = 6.59669e-07, cumulative = 6.07745e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000593997, Final residual = 6.64959e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00748258, Final residual = 9.89705e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.071509 s +other Time = 0 s +rho Equations = 0.000162 s +U Equations = 0.001185 s +Y Equations = 0.00199579 s +E Equations = 0.000485 s +p Equations = 0.001729 s +calculate parcels = 3.27432 s +chemistry correctThermo = 0.001973 s +turbulence correct = 0.000839 s +combustion correct(in Y) = 0.0629582 s +percentage of chemistry = 88.0424 % +percentage of rho/U/Y/E = 5.35288 % +========Time details of each equation======= +rhoEqn Time = 0.000274 s +rhoEqn assamble = 0.000216 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001185 s +UEqn assamble = 0.00069 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000495 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001347 s +YEqn assamble = 0.000523 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000366 s +EEqn assamble = 0.000274 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 12.8 s ClockTime = 13 s +Courant Number mean: 0.000264038 max: 0.0167394 +Time = 0.000285 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 39 new parcels + +Cloud: sprayCloud + Current number of parcels = 3593 + Current mass in system = 4.44011e-10 + Linear momentum = (2.08944e-11 -4.68191e-09 0) + |Linear momentum| = 4.68196e-09 + Linear kinetic energy = 2.59859e-08 + model1: + number of parcels added = 3593 + mass introduced = 4.4667e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.139, 519.588 + Mass transfer phase change = 2.65873e-12 + D10, D32, Dmax (mu) = 35.2142, 77.3727, 148.967 + Liquid penetration 95% mass (m) = 0.00230361 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00942522, Final residual = 2.02788e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0157464, Final residual = 4.03707e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00555978, Final residual = 4.96911e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00603562, Final residual = 3.16187e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00641063, Final residual = 2.54218e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00641065, Final residual = 2.54556e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00553442, Final residual = 4.09818e-07, No Iterations 1 +min/max(T) = 618.469, 815.713 +GAMG: Solving for p, Initial residual = 0.0721482, Final residual = 0.00118545, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.30753e-07, global = 6.8832e-07, cumulative = 6.14628e-05 +GAMG: Solving for p, Initial residual = 0.00117019, Final residual = 3.44237e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.70165e-07, global = 6.70147e-07, cumulative = 6.21329e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000600572, Final residual = 6.86549e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00744905, Final residual = 9.96874e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.093039 s +other Time = 0 s +rho Equations = 0.000168 s +U Equations = 0.001322 s +Y Equations = 0.0037143 s +E Equations = 0.000992 s +p Equations = 0.002972 s +calculate parcels = 3.33344 s +chemistry correctThermo = 0.005979 s +turbulence correct = 0.000833 s +combustion correct(in Y) = 0.0768237 s +percentage of chemistry = 82.5715 % +percentage of rho/U/Y/E = 6.65989 % +========Time details of each equation======= +rhoEqn Time = 0.000369 s +rhoEqn assamble = 0.000281 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00132 s +UEqn assamble = 0.000771 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000549 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.003031 s +YEqn assamble = 0.001058 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000566 s +YEqn correct boundary = 0 s +EEqn Time = 0.000749 s +EEqn assamble = 0.000542 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000207 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 12.95 s ClockTime = 13 s +Courant Number mean: 0.000264456 max: 0.0168185 +Time = 0.0002875 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 3639 + Current mass in system = 4.47995e-10 + Linear momentum = (2.15611e-11 -4.71538e-09 0) + |Linear momentum| = 4.71543e-09 + Linear kinetic energy = 2.61174e-08 + model1: + number of parcels added = 3639 + mass introduced = 4.50713e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.129, 520.137 + Mass transfer phase change = 2.71752e-12 + D10, D32, Dmax (mu) = 35.2068, 77.313, 149.065 + Liquid penetration 95% mass (m) = 0.00232773 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0107534, Final residual = 2.26906e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0157663, Final residual = 3.94174e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00548651, Final residual = 4.95173e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0059677, Final residual = 3.13862e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00634632, Final residual = 2.54414e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00634634, Final residual = 2.54749e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00545007, Final residual = 4.05783e-07, No Iterations 1 +min/max(T) = 618.639, 815.918 +GAMG: Solving for p, Initial residual = 0.07086, Final residual = 0.000745321, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.15847e-07, global = 6.82323e-07, cumulative = 6.28153e-05 +GAMG: Solving for p, Initial residual = 0.000729623, Final residual = 2.3145e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.77573e-07, global = 6.77561e-07, cumulative = 6.34928e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000608066, Final residual = 7.0963e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0074201, Final residual = 1.9709e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.068189 s +other Time = 0 s +rho Equations = 0.000145 s +U Equations = 0.001159 s +Y Equations = 0.00213629 s +E Equations = 0.000497 s +p Equations = 0.001989 s +calculate parcels = 3.39703 s +chemistry correctThermo = 0.002225 s +turbulence correct = 0.000906 s +combustion correct(in Y) = 0.0589507 s +percentage of chemistry = 86.4519 % +percentage of rho/U/Y/E = 5.77409 % +========Time details of each equation======= +rhoEqn Time = 0.000268 s +rhoEqn assamble = 0.000214 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001158 s +UEqn assamble = 0.000725 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000433 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001496 s +YEqn assamble = 0.00056 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.3e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000377 s +EEqn assamble = 0.000286 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 13.08 s ClockTime = 13 s +Courant Number mean: 0.000264685 max: 0.016797 +Time = 0.00029 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 3687 + Current mass in system = 4.52132e-10 + Linear momentum = (2.09674e-11 -4.75054e-09 0) + |Linear momentum| = 4.75059e-09 + Linear kinetic energy = 2.62585e-08 + model1: + number of parcels added = 3687 + mass introduced = 4.54909e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.132, 520.518 + Mass transfer phase change = 2.77694e-12 + D10, D32, Dmax (mu) = 35.3029, 77.3246, 148.709 + Liquid penetration 95% mass (m) = 0.00235058 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0106586, Final residual = 2.31157e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0157295, Final residual = 3.94786e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00542068, Final residual = 4.94407e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0059019, Final residual = 3.11969e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00627937, Final residual = 2.54625e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0062794, Final residual = 2.54957e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00535791, Final residual = 4.01381e-07, No Iterations 1 +min/max(T) = 618.815, 816.13 +GAMG: Solving for p, Initial residual = 0.0698989, Final residual = 0.000833785, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.32821e-07, global = 6.96647e-07, cumulative = 6.41895e-05 +GAMG: Solving for p, Initial residual = 0.000810858, Final residual = 2.65912e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.8496e-07, global = 6.84944e-07, cumulative = 6.48744e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000616542, Final residual = 7.34523e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00739574, Final residual = 2.01082e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.066037 s +other Time = 0 s +rho Equations = 0.000146 s +U Equations = 0.001054 s +Y Equations = 0.00205432 s +E Equations = 0.00049 s +p Equations = 0.002026 s +calculate parcels = 3.45088 s +chemistry correctThermo = 0.001976 s +turbulence correct = 0.000849 s +combustion correct(in Y) = 0.0572657 s +percentage of chemistry = 86.7176 % +percentage of rho/U/Y/E = 5.67003 % +========Time details of each equation======= +rhoEqn Time = 0.00027 s +rhoEqn assamble = 0.000216 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001053 s +UEqn assamble = 0.000637 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000416 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001462 s +YEqn assamble = 0.000541 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000113 s +YEqn correct boundary = 0 s +EEqn Time = 0.000369 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 13.2 s ClockTime = 14 s +Courant Number mean: 0.000264653 max: 0.0167437 +Time = 0.0002925 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 39 new parcels + +Cloud: sprayCloud + Current number of parcels = 3726 + Current mass in system = 4.55466e-10 + Linear momentum = (2.1008e-11 -4.77569e-09 0) + |Linear momentum| = 4.77574e-09 + Linear kinetic energy = 2.63371e-08 + model1: + number of parcels added = 3726 + mass introduced = 4.58304e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.131, 519.095 + Mass transfer phase change = 2.8374e-12 + D10, D32, Dmax (mu) = 33.3063, 77.1279, 148.714 + Liquid penetration 95% mass (m) = 0.00237383 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00992486, Final residual = 2.21813e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.01556, Final residual = 3.96381e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00539525, Final residual = 5.06609e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00585958, Final residual = 3.09734e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00622261, Final residual = 2.54589e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00622264, Final residual = 2.54927e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00531084, Final residual = 3.95049e-07, No Iterations 1 +min/max(T) = 618.997, 816.35 +GAMG: Solving for p, Initial residual = 0.0691351, Final residual = 0.000590533, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.28693e-07, global = 7.02303e-07, cumulative = 6.55767e-05 +GAMG: Solving for p, Initial residual = 0.000554469, Final residual = 9.76931e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.96831e-07, global = 6.96772e-07, cumulative = 6.62735e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000624564, Final residual = 7.59099e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00736828, Final residual = 2.04845e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.066734 s +other Time = 0 s +rho Equations = 0.000216 s +U Equations = 0.001294 s +Y Equations = 0.00220122 s +E Equations = 0.000499 s +p Equations = 0.0018 s +calculate parcels = 3.5054 s +chemistry correctThermo = 0.001894 s +turbulence correct = 0.000915 s +combustion correct(in Y) = 0.0576948 s +percentage of chemistry = 86.4548 % +percentage of rho/U/Y/E = 6.30896 % +========Time details of each equation======= +rhoEqn Time = 0.000335 s +rhoEqn assamble = 0.000267 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001294 s +UEqn assamble = 0.000817 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000477 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001585 s +YEqn assamble = 0.000586 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000118 s +YEqn correct boundary = 0 s +EEqn Time = 0.000376 s +EEqn assamble = 0.000278 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 13.32 s ClockTime = 14 s +Courant Number mean: 0.000264478 max: 0.0167425 +Time = 0.000295 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 3774 + Current mass in system = 4.59555e-10 + Linear momentum = (2.15006e-11 -4.8099e-09 0) + |Linear momentum| = 4.80995e-09 + Linear kinetic energy = 2.64711e-08 + model1: + number of parcels added = 3774 + mass introduced = 4.62453e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.126, 516.264 + Mass transfer phase change = 2.89853e-12 + D10, D32, Dmax (mu) = 33.3278, 77.1069, 148.718 + Liquid penetration 95% mass (m) = 0.00239873 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00933413, Final residual = 2.20323e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0152168, Final residual = 3.89207e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00534704, Final residual = 5.16111e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00579549, Final residual = 3.05652e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00616024, Final residual = 2.54658e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00616027, Final residual = 2.54992e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00523018, Final residual = 3.85918e-07, No Iterations 1 +min/max(T) = 619.183, 816.568 +GAMG: Solving for p, Initial residual = 0.066268, Final residual = 0.000545223, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.36158e-07, global = 7.10068e-07, cumulative = 6.69836e-05 +GAMG: Solving for p, Initial residual = 0.000512742, Final residual = 6.25305e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.04622e-07, global = 7.04583e-07, cumulative = 6.76881e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000633158, Final residual = 7.85054e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00734312, Final residual = 2.08803e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.090294 s +other Time = 1e-06 s +rho Equations = 0.000161 s +U Equations = 0.001199 s +Y Equations = 0.00238603 s +E Equations = 0.000609 s +p Equations = 0.002365 s +calculate parcels = 3.57514 s +chemistry correctThermo = 0.002791 s +turbulence correct = 0.001057 s +combustion correct(in Y) = 0.079537 s +percentage of chemistry = 88.0867 % +percentage of rho/U/Y/E = 4.82317 % +========Time details of each equation======= +rhoEqn Time = 0.000312 s +rhoEqn assamble = 0.000247 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001198 s +UEqn assamble = 0.000692 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000506 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001742 s +YEqn assamble = 0.000655 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000195 s +YEqn correct boundary = 0 s +EEqn Time = 0.000454 s +EEqn assamble = 0.00034 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 13.48 s ClockTime = 14 s +Courant Number mean: 0.000264142 max: 0.0166958 +Time = 0.0002975 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 3824 + Current mass in system = 4.63806e-10 + Linear momentum = (2.19993e-11 -4.8459e-09 0) + |Linear momentum| = 4.84595e-09 + Linear kinetic energy = 2.66161e-08 + model1: + number of parcels added = 3824 + mass introduced = 4.66766e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.138, 513.533 + Mass transfer phase change = 2.96043e-12 + D10, D32, Dmax (mu) = 33.4173, 77.0383, 148.723 + Liquid penetration 95% mass (m) = 0.00242324 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00915718, Final residual = 2.17808e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.014795, Final residual = 3.82493e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0052782, Final residual = 5.01238e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00574249, Final residual = 3.05054e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00610344, Final residual = 2.54368e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00610347, Final residual = 2.54699e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0051708, Final residual = 3.95104e-07, No Iterations 1 +min/max(T) = 619.435, 816.79 +GAMG: Solving for p, Initial residual = 0.0640427, Final residual = 0.00054633, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.46209e-07, global = 7.17882e-07, cumulative = 6.8406e-05 +GAMG: Solving for p, Initial residual = 0.000514964, Final residual = 4.59751e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.13542e-07, global = 7.13512e-07, cumulative = 6.91195e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000641332, Final residual = 8.11248e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00731569, Final residual = 2.12787e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.103488 s +other Time = 1e-06 s +rho Equations = 0.000125 s +U Equations = 0.000975 s +Y Equations = 0.00240132 s +E Equations = 0.000619 s +p Equations = 0.002199 s +calculate parcels = 3.6408 s +chemistry correctThermo = 0.002785 s +turbulence correct = 0.00113 s +combustion correct(in Y) = 0.0930857 s +percentage of chemistry = 89.9483 % +percentage of rho/U/Y/E = 3.98144 % +========Time details of each equation======= +rhoEqn Time = 0.000264 s +rhoEqn assamble = 0.00021 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000974 s +UEqn assamble = 0.000567 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000407 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001696 s +YEqn assamble = 0.000676 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000138 s +YEqn correct boundary = 0 s +EEqn Time = 0.000465 s +EEqn assamble = 0.00035 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 13.65 s ClockTime = 14 s +Courant Number mean: 0.000263723 max: 0.0166876 +Time = 0.0003 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 55 new parcels + +Cloud: sprayCloud + Current number of parcels = 3879 + Current mass in system = 4.6848e-10 + Linear momentum = (2.2798e-11 -4.88696e-09 0) + |Linear momentum| = 4.88702e-09 + Linear kinetic energy = 2.67918e-08 + model1: + number of parcels added = 3879 + mass introduced = 4.71503e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.138, 512.191 + Mass transfer phase change = 3.02307e-12 + D10, D32, Dmax (mu) = 33.5256, 77.0948, 148.727 + Liquid penetration 95% mass (m) = 0.00244317 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00849354, Final residual = 2.04569e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0143491, Final residual = 3.7053e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00522968, Final residual = 4.94228e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00568922, Final residual = 3.02086e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00604516, Final residual = 2.53831e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00604519, Final residual = 2.54141e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00510668, Final residual = 3.93623e-07, No Iterations 1 +min/max(T) = 619.716, 817.011 +GAMG: Solving for p, Initial residual = 0.0613298, Final residual = 0.000487564, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.52066e-07, global = 7.26747e-07, cumulative = 6.98463e-05 +GAMG: Solving for p, Initial residual = 0.000460217, Final residual = 3.69264e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.21999e-07, global = 7.21974e-07, cumulative = 7.05683e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000649396, Final residual = 8.38586e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00728668, Final residual = 2.17029e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.090445 s +other Time = 0 s +rho Equations = 0.000137 s +U Equations = 0.001046 s +Y Equations = 0.00240122 s +E Equations = 0.000608 s +p Equations = 0.00225 s +calculate parcels = 3.71354 s +chemistry correctThermo = 0.002767 s +turbulence correct = 0.001087 s +combustion correct(in Y) = 0.0799308 s +percentage of chemistry = 88.375 % +percentage of rho/U/Y/E = 4.6351 % +========Time details of each equation======= +rhoEqn Time = 0.000298 s +rhoEqn assamble = 0.000228 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001045 s +UEqn assamble = 0.000614 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000431 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001813 s +YEqn assamble = 0.000682 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000221 s +YEqn correct boundary = 0 s +EEqn Time = 0.000453 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 13.9 s ClockTime = 14 s +Courant Number mean: 0.000263183 max: 0.0166583 +Time = 0.0003025 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 59 new parcels + +Cloud: sprayCloud + Current number of parcels = 3938 + Current mass in system = 4.73504e-10 + Linear momentum = (2.2338e-11 -4.93213e-09 0) + |Linear momentum| = 4.93218e-09 + Linear kinetic energy = 2.6992e-08 + model1: + number of parcels added = 3938 + mass introduced = 4.7659e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.125, 512.126 + Mass transfer phase change = 3.08656e-12 + D10, D32, Dmax (mu) = 33.6443, 77.1371, 148.961 + Liquid penetration 95% mass (m) = 0.00246417 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00836975, Final residual = 2.00994e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0138652, Final residual = 3.5854e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00519804, Final residual = 4.87476e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00564851, Final residual = 2.99705e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00599696, Final residual = 2.53937e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00599699, Final residual = 2.54251e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00506463, Final residual = 3.91645e-07, No Iterations 1 +min/max(T) = 620.017, 817.235 +GAMG: Solving for p, Initial residual = 0.0595658, Final residual = 0.000498513, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.63913e-07, global = 7.35258e-07, cumulative = 7.13035e-05 +GAMG: Solving for p, Initial residual = 0.00047268, Final residual = 6.03612e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.31843e-07, global = 7.318e-07, cumulative = 7.20353e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000657187, Final residual = 8.66247e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00725392, Final residual = 2.2116e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.089056 s +other Time = 0 s +rho Equations = 0.00016 s +U Equations = 0.001268 s +Y Equations = 0.00204523 s +E Equations = 0.000495 s +p Equations = 0.00176 s +calculate parcels = 3.78346 s +chemistry correctThermo = 0.002002 s +turbulence correct = 0.000852 s +combustion correct(in Y) = 0.0802838 s +percentage of chemistry = 90.1498 % +percentage of rho/U/Y/E = 4.45588 % +========Time details of each equation======= +rhoEqn Time = 0.000274 s +rhoEqn assamble = 0.000216 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001268 s +UEqn assamble = 0.000775 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000493 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001342 s +YEqn assamble = 0.000521 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 5.9e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000379 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000102 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 14.06 s ClockTime = 14 s +Courant Number mean: 0.000262528 max: 0.0166401 +Time = 0.000305 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 40 new parcels + +Cloud: sprayCloud + Current number of parcels = 3978 + Current mass in system = 4.76898e-10 + Linear momentum = (2.17411e-11 -4.95755e-09 0) + |Linear momentum| = 4.9576e-09 + Linear kinetic energy = 2.70722e-08 + model1: + number of parcels added = 3978 + mass introduced = 4.80049e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.127, 512.047 + Mass transfer phase change = 3.15093e-12 + D10, D32, Dmax (mu) = 33.7333, 77.1205, 148.737 + Liquid penetration 95% mass (m) = 0.00248947 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0080988, Final residual = 1.88796e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0133628, Final residual = 3.44905e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00516946, Final residual = 4.91334e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00560588, Final residual = 2.94587e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00594192, Final residual = 2.53996e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00594195, Final residual = 2.54307e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00502327, Final residual = 3.87506e-07, No Iterations 1 +min/max(T) = 620.35, 817.462 +GAMG: Solving for p, Initial residual = 0.0587185, Final residual = 0.000656987, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.83795e-07, global = 7.4969e-07, cumulative = 7.2785e-05 +GAMG: Solving for p, Initial residual = 0.000626626, Final residual = 8.59536e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.41965e-07, global = 7.41902e-07, cumulative = 7.35269e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000665358, Final residual = 8.94714e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00722144, Final residual = 2.25157e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.076586 s +other Time = 0 s +rho Equations = 0.000154 s +U Equations = 0.001204 s +Y Equations = 0.00203169 s +E Equations = 0.000495 s +p Equations = 0.001813 s +calculate parcels = 3.85475 s +chemistry correctThermo = 0.00199 s +turbulence correct = 0.000912 s +combustion correct(in Y) = 0.0678023 s +percentage of chemistry = 88.5309 % +percentage of rho/U/Y/E = 5.07233 % +========Time details of each equation======= +rhoEqn Time = 0.000271 s +rhoEqn assamble = 0.000213 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001203 s +UEqn assamble = 0.000694 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000509 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001377 s +YEqn assamble = 0.000518 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.2e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000377 s +EEqn assamble = 0.000282 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 14.2 s ClockTime = 15 s +Courant Number mean: 0.000261626 max: 0.0165796 +Time = 0.0003075 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 34 new parcels + +Cloud: sprayCloud + Current number of parcels = 4012 + Current mass in system = 4.79755e-10 + Linear momentum = (2.22773e-11 -4.97646e-09 0) + |Linear momentum| = 4.97651e-09 + Linear kinetic energy = 2.71131e-08 + model1: + number of parcels added = 4012 + mass introduced = 4.82971e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.144, 511.955 + Mass transfer phase change = 3.21628e-12 + D10, D32, Dmax (mu) = 33.8126, 77.0812, 148.741 + Liquid penetration 95% mass (m) = 0.00251098 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00754291, Final residual = 9.34833e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0128106, Final residual = 3.37065e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0051564, Final residual = 5.03842e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00557401, Final residual = 2.93859e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00589446, Final residual = 2.53925e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00589449, Final residual = 2.54224e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00501783, Final residual = 3.82757e-07, No Iterations 1 +min/max(T) = 620.719, 817.694 +GAMG: Solving for p, Initial residual = 0.056232, Final residual = 0.000538981, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.91029e-07, global = 7.60354e-07, cumulative = 7.42873e-05 +GAMG: Solving for p, Initial residual = 0.000512475, Final residual = 4.81199e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.53297e-07, global = 7.5326e-07, cumulative = 7.50405e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000673343, Final residual = 9.23049e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00718781, Final residual = 2.2893e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.08896 s +other Time = 1e-06 s +rho Equations = 0.00016 s +U Equations = 0.00113 s +Y Equations = 0.00246279 s +E Equations = 0.000602 s +p Equations = 0.002202 s +calculate parcels = 3.93203 s +chemistry correctThermo = 0.002779 s +turbulence correct = 0.001073 s +combustion correct(in Y) = 0.0783562 s +percentage of chemistry = 88.0803 % +percentage of rho/U/Y/E = 4.89522 % +========Time details of each equation======= +rhoEqn Time = 0.000307 s +rhoEqn assamble = 0.000243 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001127 s +UEqn assamble = 0.00069 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000437 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001807 s +YEqn assamble = 0.000678 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000207 s +YEqn correct boundary = 0 s +EEqn Time = 0.000448 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 14.37 s ClockTime = 15 s +Courant Number mean: 0.000260547 max: 0.0165333 +Time = 0.00031 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 47 new parcels + +Cloud: sprayCloud + Current number of parcels = 4059 + Current mass in system = 4.83693e-10 + Linear momentum = (2.2693e-11 -5.00836e-09 0) + |Linear momentum| = 5.00841e-09 + Linear kinetic energy = 2.72326e-08 + model1: + number of parcels added = 4059 + mass introduced = 4.86976e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.13, 511.853 + Mass transfer phase change = 3.28269e-12 + D10, D32, Dmax (mu) = 33.9054, 77.1212, 149.183 + Liquid penetration 95% mass (m) = 0.00253205 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00683047, Final residual = 8.26368e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.012221, Final residual = 3.26202e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00514615, Final residual = 4.99319e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00554268, Final residual = 2.89915e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00584524, Final residual = 2.53468e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00584527, Final residual = 2.53764e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00496794, Final residual = 3.69801e-07, No Iterations 1 +min/max(T) = 621.077, 817.928 +GAMG: Solving for p, Initial residual = 0.0543576, Final residual = 0.000476192, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.98072e-07, global = 7.6998e-07, cumulative = 7.58105e-05 +GAMG: Solving for p, Initial residual = 0.000457823, Final residual = 3.15457e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.6547e-07, global = 7.65446e-07, cumulative = 7.65759e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000681036, Final residual = 9.52044e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00715228, Final residual = 2.32763e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.092155 s +other Time = 0 s +rho Equations = 0.000155 s +U Equations = 0.001137 s +Y Equations = 0.00349747 s +E Equations = 0.000961 s +p Equations = 0.003656 s +calculate parcels = 4.01366 s +chemistry correctThermo = 0.005176 s +turbulence correct = 0.001712 s +combustion correct(in Y) = 0.0756555 s +percentage of chemistry = 82.096 % +percentage of rho/U/Y/E = 6.24 % +========Time details of each equation======= +rhoEqn Time = 0.000429 s +rhoEqn assamble = 0.000325 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000104 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001134 s +UEqn assamble = 0.000702 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000432 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002849 s +YEqn assamble = 0.001063 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000526 s +YEqn correct boundary = 0 s +EEqn Time = 0.000729 s +EEqn assamble = 0.000528 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000201 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 14.54 s ClockTime = 15 s +Courant Number mean: 0.000259405 max: 0.0164916 +Time = 0.0003125 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 34 new parcels + +Cloud: sprayCloud + Current number of parcels = 4093 + Current mass in system = 4.86515e-10 + Linear momentum = (2.31087e-11 -5.0268e-09 0) + |Linear momentum| = 5.02686e-09 + Linear kinetic energy = 2.72707e-08 + model1: + number of parcels added = 4093 + mass introduced = 4.89865e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.124, 511.74 + Mass transfer phase change = 3.35016e-12 + D10, D32, Dmax (mu) = 33.9741, 77.0994, 148.926 + Liquid penetration 95% mass (m) = 0.00255554 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0067549, Final residual = 8.22162e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.01167, Final residual = 3.10884e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0051334, Final residual = 4.96039e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00551218, Final residual = 2.88255e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00579975, Final residual = 2.53024e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00579978, Final residual = 2.53317e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0049413, Final residual = 3.61143e-07, No Iterations 1 +min/max(T) = 621.46, 818.164 +GAMG: Solving for p, Initial residual = 0.0527249, Final residual = 0.000418439, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.07661e-07, global = 7.82171e-07, cumulative = 7.73581e-05 +GAMG: Solving for p, Initial residual = 0.000401228, Final residual = 2.32564e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.77679e-07, global = 7.7766e-07, cumulative = 7.81358e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000688478, Final residual = 9.80291e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00711551, Final residual = 2.36282e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.095774 s +other Time = 1e-06 s +rho Equations = 0.000162 s +U Equations = 0.001145 s +Y Equations = 0.00239779 s +E Equations = 0.000613 s +p Equations = 0.002642 s +calculate parcels = 4.09807 s +chemistry correctThermo = 0.002772 s +turbulence correct = 0.00171 s +combustion correct(in Y) = 0.0841292 s +percentage of chemistry = 87.8414 % +percentage of rho/U/Y/E = 4.50831 % +========Time details of each equation======= +rhoEqn Time = 0.000389 s +rhoEqn assamble = 0.000301 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001143 s +UEqn assamble = 0.000716 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000427 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001737 s +YEqn assamble = 0.000644 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000183 s +YEqn correct boundary = 0 s +EEqn Time = 0.000456 s +EEqn assamble = 0.000339 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 14.72 s ClockTime = 15 s +Courant Number mean: 0.000258141 max: 0.0164448 +Time = 0.000315 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 61 new parcels + +Cloud: sprayCloud + Current number of parcels = 4154 + Current mass in system = 4.91585e-10 + Linear momentum = (2.2143e-11 -5.07215e-09 0) + |Linear momentum| = 5.07219e-09 + Linear kinetic energy = 2.74713e-08 + model1: + number of parcels added = 4154 + mass introduced = 4.95003e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.131, 511.618 + Mass transfer phase change = 3.41872e-12 + D10, D32, Dmax (mu) = 34.0882, 77.1643, 148.756 + Liquid penetration 95% mass (m) = 0.00257817 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00665386, Final residual = 7.91367e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0112298, Final residual = 3.00747e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0051255, Final residual = 4.97426e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00548392, Final residual = 2.88558e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00575402, Final residual = 2.53354e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00575405, Final residual = 2.53652e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00493018, Final residual = 3.55496e-07, No Iterations 1 +min/max(T) = 621.867, 818.403 +GAMG: Solving for p, Initial residual = 0.0515406, Final residual = 0.000456273, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.23262e-07, global = 7.95739e-07, cumulative = 7.89315e-05 +GAMG: Solving for p, Initial residual = 0.000440294, Final residual = 8.02499e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.90299e-07, global = 7.90236e-07, cumulative = 7.97218e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000695368, Final residual = 1.00697e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00707655, Final residual = 2.3921e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.07891 s +other Time = 0 s +rho Equations = 0.000151 s +U Equations = 0.00095 s +Y Equations = 0.00261106 s +E Equations = 0.000652 s +p Equations = 0.002686 s +calculate parcels = 4.17489 s +chemistry correctThermo = 0.002854 s +turbulence correct = 0.001204 s +combustion correct(in Y) = 0.0676099 s +percentage of chemistry = 85.6798 % +percentage of rho/U/Y/E = 5.53043 % +========Time details of each equation======= +rhoEqn Time = 0.000327 s +rhoEqn assamble = 0.000257 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000949 s +UEqn assamble = 0.000589 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00036 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002053 s +YEqn assamble = 0.000712 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000264 s +YEqn correct boundary = 0 s +EEqn Time = 0.00047 s +EEqn assamble = 0.000353 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 14.88 s ClockTime = 15 s +Courant Number mean: 0.000256815 max: 0.016425 +Time = 0.0003175 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 4200 + Current mass in system = 4.95404e-10 + Linear momentum = (2.22879e-11 -5.10238e-09 0) + |Linear momentum| = 5.10243e-09 + Linear kinetic energy = 2.75803e-08 + model1: + number of parcels added = 4200 + mass introduced = 4.98893e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.125, 511.487 + Mass transfer phase change = 3.48834e-12 + D10, D32, Dmax (mu) = 34.16, 77.1229, 148.76 + Liquid penetration 95% mass (m) = 0.00260024 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0064285, Final residual = 7.33311e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.010955, Final residual = 2.92902e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00511022, Final residual = 4.93901e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00545413, Final residual = 2.86815e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00571183, Final residual = 2.53342e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00571186, Final residual = 2.53638e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00489147, Final residual = 3.42257e-07, No Iterations 1 +min/max(T) = 622.252, 818.645 +GAMG: Solving for p, Initial residual = 0.0497989, Final residual = 0.000451377, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.35627e-07, global = 8.07687e-07, cumulative = 8.05294e-05 +GAMG: Solving for p, Initial residual = 0.000438035, Final residual = 7.26524e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.02418e-07, global = 8.0236e-07, cumulative = 8.13318e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000701943, Final residual = 1.03343e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00703575, Final residual = 2.41928e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.092623 s +other Time = 0 s +rho Equations = 0.000143 s +U Equations = 0.000951 s +Y Equations = 0.00237335 s +E Equations = 0.000612 s +p Equations = 0.002152 s +calculate parcels = 4.25157 s +chemistry correctThermo = 0.002774 s +turbulence correct = 0.001014 s +combustion correct(in Y) = 0.0824156 s +percentage of chemistry = 88.9797 % +percentage of rho/U/Y/E = 4.40425 % +========Time details of each equation======= +rhoEqn Time = 0.000281 s +rhoEqn assamble = 0.00022 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000951 s +UEqn assamble = 0.00059 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000361 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001814 s +YEqn assamble = 0.000682 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000218 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000338 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 15.05 s ClockTime = 15 s +Courant Number mean: 0.000255495 max: 0.0164065 +Time = 0.00032 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 4248 + Current mass in system = 4.99379e-10 + Linear momentum = (2.30377e-11 -5.13437e-09 0) + |Linear momentum| = 5.13443e-09 + Linear kinetic energy = 2.76998e-08 + model1: + number of parcels added = 4248 + mass introduced = 5.02938e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.135, 511.348 + Mass transfer phase change = 3.55895e-12 + D10, D32, Dmax (mu) = 34.2488, 77.1243, 148.765 + Liquid penetration 95% mass (m) = 0.00262303 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0066389, Final residual = 7.25627e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0109976, Final residual = 2.90576e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00508774, Final residual = 4.87192e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00542211, Final residual = 2.82567e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00567134, Final residual = 2.52896e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00567136, Final residual = 2.53189e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0048534, Final residual = 3.28805e-07, No Iterations 1 +min/max(T) = 622.636, 818.889 +GAMG: Solving for p, Initial residual = 0.0481803, Final residual = 0.000417273, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.44056e-07, global = 8.21134e-07, cumulative = 8.21529e-05 +GAMG: Solving for p, Initial residual = 0.000402898, Final residual = 4.37477e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.13904e-07, global = 8.13869e-07, cumulative = 8.29668e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000708734, Final residual = 1.05978e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00699523, Final residual = 2.4443e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.09454 s +other Time = 1e-06 s +rho Equations = 0.000162 s +U Equations = 0.001131 s +Y Equations = 0.0023911 s +E Equations = 0.000601 s +p Equations = 0.002253 s +calculate parcels = 4.33158 s +chemistry correctThermo = 0.002792 s +turbulence correct = 0.001239 s +combustion correct(in Y) = 0.0837689 s +percentage of chemistry = 88.6068 % +percentage of rho/U/Y/E = 4.53258 % +========Time details of each equation======= +rhoEqn Time = 0.00031 s +rhoEqn assamble = 0.000246 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00113 s +UEqn assamble = 0.000694 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000436 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001725 s +YEqn assamble = 0.000639 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000169 s +YEqn correct boundary = 0 s +EEqn Time = 0.000445 s +EEqn assamble = 0.000333 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 15.22 s ClockTime = 16 s +Courant Number mean: 0.000254123 max: 0.016356 +Time = 0.0003225 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 41 new parcels + +Cloud: sprayCloud + Current number of parcels = 4289 + Current mass in system = 5.02755e-10 + Linear momentum = (2.3766e-11 -5.15914e-09 0) + |Linear momentum| = 5.1592e-09 + Linear kinetic energy = 2.77755e-08 + model1: + number of parcels added = 4289 + mass introduced = 5.06386e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.134, 511.201 + Mass transfer phase change = 3.63057e-12 + D10, D32, Dmax (mu) = 34.3125, 77.064, 148.77 + Liquid penetration 95% mass (m) = 0.0026444 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00663668, Final residual = 7.03116e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0111486, Final residual = 2.94255e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00512415, Final residual = 4.99285e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00539121, Final residual = 2.86449e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00563079, Final residual = 2.52668e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00563081, Final residual = 2.52955e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00486229, Final residual = 3.27042e-07, No Iterations 1 +min/max(T) = 623.068, 819.14 +GAMG: Solving for p, Initial residual = 0.0469505, Final residual = 0.000419318, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.56352e-07, global = 8.31558e-07, cumulative = 8.37984e-05 +GAMG: Solving for p, Initial residual = 0.000404683, Final residual = 4.46453e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.25475e-07, global = 8.25436e-07, cumulative = 8.46238e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000715499, Final residual = 1.08481e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00695498, Final residual = 2.46419e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.0905 s +other Time = 0 s +rho Equations = 0.000158 s +U Equations = 0.001134 s +Y Equations = 0.00255662 s +E Equations = 0.00065 s +p Equations = 0.00222 s +calculate parcels = 4.41487 s +chemistry correctThermo = 0.002757 s +turbulence correct = 0.000943 s +combustion correct(in Y) = 0.0798914 s +percentage of chemistry = 88.2778 % +percentage of rho/U/Y/E = 4.97085 % +========Time details of each equation======= +rhoEqn Time = 0.000301 s +rhoEqn assamble = 0.000227 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001134 s +UEqn assamble = 0.000702 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000432 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001839 s +YEqn assamble = 0.000714 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000147 s +YEqn correct boundary = 0 s +EEqn Time = 0.00049 s +EEqn assamble = 0.00037 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00012 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 15.4 s ClockTime = 16 s +Courant Number mean: 0.000252648 max: 0.016312 +Time = 0.000325 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 61 new parcels + +Cloud: sprayCloud + Current number of parcels = 4350 + Current mass in system = 5.07784e-10 + Linear momentum = (2.45673e-11 -5.20338e-09 0) + |Linear momentum| = 5.20344e-09 + Linear kinetic energy = 2.79689e-08 + model1: + number of parcels added = 4350 + mass introduced = 5.11487e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.13, 511.261 + Mass transfer phase change = 3.70314e-12 + D10, D32, Dmax (mu) = 34.4136, 77.1195, 148.821 + Liquid penetration 95% mass (m) = 0.00266706 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00624461, Final residual = 6.58776e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0112985, Final residual = 2.9977e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00510628, Final residual = 4.94621e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00535913, Final residual = 2.83737e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00559141, Final residual = 2.52189e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00559143, Final residual = 2.52473e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00485084, Final residual = 3.24306e-07, No Iterations 1 +min/max(T) = 623.537, 819.393 +GAMG: Solving for p, Initial residual = 0.0448745, Final residual = 0.000413779, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.67747e-07, global = 8.43996e-07, cumulative = 8.54678e-05 +GAMG: Solving for p, Initial residual = 0.00040136, Final residual = 4.96659e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.36596e-07, global = 8.36554e-07, cumulative = 8.63043e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000721822, Final residual = 1.10802e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00691284, Final residual = 2.47783e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.069538 s +other Time = 0 s +rho Equations = 0.000159 s +U Equations = 0.001114 s +Y Equations = 0.00251751 s +E Equations = 0.000574 s +p Equations = 0.001976 s +calculate parcels = 4.47624 s +chemistry correctThermo = 0.002024 s +turbulence correct = 0.000917 s +combustion correct(in Y) = 0.0600625 s +percentage of chemistry = 86.3736 % +percentage of rho/U/Y/E = 6.27644 % +========Time details of each equation======= +rhoEqn Time = 0.000289 s +rhoEqn assamble = 0.000229 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001113 s +UEqn assamble = 0.000714 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000399 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001888 s +YEqn assamble = 0.000808 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000191 s +YEqn correct boundary = 0 s +EEqn Time = 0.000409 s +EEqn assamble = 0.000302 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000107 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 15.53 s ClockTime = 16 s +Courant Number mean: 0.000251164 max: 0.01628 +Time = 0.0003275 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 47 new parcels + +Cloud: sprayCloud + Current number of parcels = 4397 + Current mass in system = 5.11656e-10 + Linear momentum = (2.40433e-11 -5.23382e-09 0) + |Linear momentum| = 5.23387e-09 + Linear kinetic energy = 2.80785e-08 + model1: + number of parcels added = 4397 + mass introduced = 5.15432e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.133, 513.465 + Mass transfer phase change = 3.77653e-12 + D10, D32, Dmax (mu) = 34.4876, 77.1225, 148.78 + Liquid penetration 95% mass (m) = 0.002689 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00605954, Final residual = 6.34888e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0113553, Final residual = 3.00731e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00500347, Final residual = 4.56611e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00531915, Final residual = 2.72748e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00555085, Final residual = 2.51045e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00555087, Final residual = 2.51326e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00477166, Final residual = 3.08287e-07, No Iterations 1 +min/max(T) = 623.987, 819.647 +GAMG: Solving for p, Initial residual = 0.0430342, Final residual = 0.000432005, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.79423e-07, global = 8.54212e-07, cumulative = 8.71586e-05 +GAMG: Solving for p, Initial residual = 0.000416635, Final residual = 3.09968e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.45883e-07, global = 8.45854e-07, cumulative = 8.80044e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000728218, Final residual = 1.13193e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00687043, Final residual = 2.49194e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.067285 s +other Time = 0 s +rho Equations = 0.000158 s +U Equations = 0.001159 s +Y Equations = 0.00217849 s +E Equations = 0.000485 s +p Equations = 0.001874 s +calculate parcels = 4.53799 s +chemistry correctThermo = 0.001993 s +turbulence correct = 0.000891 s +combustion correct(in Y) = 0.0583755 s +percentage of chemistry = 86.7586 % +percentage of rho/U/Y/E = 5.91586 % +========Time details of each equation======= +rhoEqn Time = 0.000286 s +rhoEqn assamble = 0.00023 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001157 s +UEqn assamble = 0.000763 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000394 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001616 s +YEqn assamble = 0.000645 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000135 s +YEqn correct boundary = 0 s +EEqn Time = 0.000366 s +EEqn assamble = 0.000274 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 15.66 s ClockTime = 16 s +Courant Number mean: 0.000249701 max: 0.0162181 +Time = 0.00033 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 37 new parcels + +Cloud: sprayCloud + Current number of parcels = 4434 + Current mass in system = 5.14679e-10 + Linear momentum = (2.31222e-11 -5.25411e-09 0) + |Linear momentum| = 5.25416e-09 + Linear kinetic energy = 2.81273e-08 + model1: + number of parcels added = 4434 + mass introduced = 5.1853e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.137, 515.349 + Mass transfer phase change = 3.85071e-12 + D10, D32, Dmax (mu) = 34.545, 77.1005, 148.785 + Liquid penetration 95% mass (m) = 0.00271134 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00624306, Final residual = 6.67503e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0113956, Final residual = 3.01151e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0049752, Final residual = 4.54471e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0052784, Final residual = 2.63957e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00550861, Final residual = 2.49897e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00550864, Final residual = 2.50174e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00475859, Final residual = 3.11312e-07, No Iterations 1 +min/max(T) = 624.472, 819.907 +GAMG: Solving for p, Initial residual = 0.0406465, Final residual = 0.000414234, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.91366e-07, global = 8.62084e-07, cumulative = 8.88665e-05 +GAMG: Solving for p, Initial residual = 0.000400277, Final residual = 3.23721e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.54977e-07, global = 8.54945e-07, cumulative = 8.97214e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000734379, Final residual = 1.15464e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00682839, Final residual = 2.50331e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.07685 s +other Time = 1e-06 s +rho Equations = 0.000143 s +U Equations = 0.001 s +Y Equations = 0.00241535 s +E Equations = 0.000603 s +p Equations = 0.00224 s +calculate parcels = 4.60565 s +chemistry correctThermo = 0.002801 s +turbulence correct = 0.001041 s +combustion correct(in Y) = 0.0664266 s +percentage of chemistry = 86.4368 % +percentage of rho/U/Y/E = 5.41491 % +========Time details of each equation======= +rhoEqn Time = 0.000289 s +rhoEqn assamble = 0.000228 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000999 s +UEqn assamble = 0.000636 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000363 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001817 s +YEqn assamble = 0.000654 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000217 s +YEqn correct boundary = 0 s +EEqn Time = 0.000445 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 15.8 s ClockTime = 16 s +Courant Number mean: 0.000248188 max: 0.0161664 +Time = 0.0003325 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 39 new parcels + +Cloud: sprayCloud + Current number of parcels = 4473 + Current mass in system = 5.17845e-10 + Linear momentum = (2.29312e-11 -5.27598e-09 0) + |Linear momentum| = 5.27603e-09 + Linear kinetic energy = 2.81856e-08 + model1: + number of parcels added = 4473 + mass introduced = 5.21771e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.143, 516.937 + Mass transfer phase change = 3.92561e-12 + D10, D32, Dmax (mu) = 34.4938, 77.044, 148.79 + Liquid penetration 95% mass (m) = 0.00273384 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00611284, Final residual = 6.48743e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0114837, Final residual = 3.04699e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00496831, Final residual = 4.48568e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00523862, Final residual = 2.6027e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00546785, Final residual = 2.48198e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00546787, Final residual = 2.48471e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00473604, Final residual = 3.14366e-07, No Iterations 1 +min/max(T) = 624.974, 820.17 +GAMG: Solving for p, Initial residual = 0.0383007, Final residual = 0.000386201, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.98214e-07, global = 8.72462e-07, cumulative = 9.05939e-05 +GAMG: Solving for p, Initial residual = 0.000373246, Final residual = 3.46765e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.63406e-07, global = 8.63374e-07, cumulative = 9.14573e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000739954, Final residual = 1.17545e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00678454, Final residual = 2.5095e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.090437 s +other Time = 1e-06 s +rho Equations = 0.000162 s +U Equations = 0.001134 s +Y Equations = 0.00206223 s +E Equations = 0.000502 s +p Equations = 0.002184 s +calculate parcels = 4.69135 s +chemistry correctThermo = 0.002104 s +turbulence correct = 0.001069 s +combustion correct(in Y) = 0.0810228 s +percentage of chemistry = 89.5903 % +percentage of rho/U/Y/E = 4.26842 % +========Time details of each equation======= +rhoEqn Time = 0.000306 s +rhoEqn assamble = 0.000244 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001134 s +UEqn assamble = 0.000701 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000433 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001412 s +YEqn assamble = 0.000538 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.5e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.00038 s +EEqn assamble = 0.000284 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 15.98 s ClockTime = 16 s +Courant Number mean: 0.000246715 max: 0.0161561 +Time = 0.000335 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 58 new parcels + +Cloud: sprayCloud + Current number of parcels = 4531 + Current mass in system = 5.22567e-10 + Linear momentum = (2.32612e-11 -5.31632e-09 0) + |Linear momentum| = 5.31637e-09 + Linear kinetic energy = 2.83548e-08 + model1: + number of parcels added = 4531 + mass introduced = 5.26568e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.13, 518.251 + Mass transfer phase change = 4.00113e-12 + D10, D32, Dmax (mu) = 34.5694, 77.0939, 148.795 + Liquid penetration 95% mass (m) = 0.00275544 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00581595, Final residual = 6.35998e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0114679, Final residual = 3.0204e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00494768, Final residual = 4.40407e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00519157, Final residual = 2.55597e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00542415, Final residual = 2.46318e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00542418, Final residual = 2.46588e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00470346, Final residual = 3.14501e-07, No Iterations 1 +min/max(T) = 625.488, 820.434 +GAMG: Solving for p, Initial residual = 0.036349, Final residual = 0.000343365, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.01446e-07, global = 8.80313e-07, cumulative = 9.23376e-05 +GAMG: Solving for p, Initial residual = 0.00033142, Final residual = 2.82263e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.70369e-07, global = 8.70345e-07, cumulative = 9.32079e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000745506, Final residual = 1.1952e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00674031, Final residual = 2.51188e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.095662 s +other Time = 0 s +rho Equations = 0.000165 s +U Equations = 0.001162 s +Y Equations = 0.00203158 s +E Equations = 0.000492 s +p Equations = 0.001843 s +calculate parcels = 4.77132 s +chemistry correctThermo = 0.002076 s +turbulence correct = 0.000892 s +combustion correct(in Y) = 0.0868054 s +percentage of chemistry = 90.7418 % +percentage of rho/U/Y/E = 4.02519 % +========Time details of each equation======= +rhoEqn Time = 0.000287 s +rhoEqn assamble = 0.000228 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001161 s +UEqn assamble = 0.000688 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000473 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001363 s +YEqn assamble = 0.000529 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 7.6e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000375 s +EEqn assamble = 0.000279 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 16.15 s ClockTime = 17 s +Courant Number mean: 0.000245303 max: 0.0162024 +Time = 0.0003375 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 43 new parcels + +Cloud: sprayCloud + Current number of parcels = 4574 + Current mass in system = 5.2608e-10 + Linear momentum = (2.32832e-11 -5.34248e-09 0) + |Linear momentum| = 5.34253e-09 + Linear kinetic energy = 2.84405e-08 + model1: + number of parcels added = 4574 + mass introduced = 5.30157e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.13, 519.307 + Mass transfer phase change = 4.07719e-12 + D10, D32, Dmax (mu) = 34.6175, 77.0914, 148.8 + Liquid penetration 95% mass (m) = 0.00277726 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00589241, Final residual = 6.87086e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0114429, Final residual = 3.00831e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00488994, Final residual = 4.24403e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00514426, Final residual = 2.4732e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00538323, Final residual = 2.43882e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00538325, Final residual = 2.44146e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00465052, Final residual = 3.08192e-07, No Iterations 1 +min/max(T) = 625.988, 820.702 +GAMG: Solving for p, Initial residual = 0.0358742, Final residual = 0.000361675, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.11253e-07, global = 8.8552e-07, cumulative = 9.40935e-05 +GAMG: Solving for p, Initial residual = 0.0003511, Final residual = 3.33349e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.7677e-07, global = 8.76734e-07, cumulative = 9.49702e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000750748, Final residual = 1.21453e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00669555, Final residual = 2.51348e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.094388 s +other Time = 0 s +rho Equations = 0.000183 s +U Equations = 0.00114 s +Y Equations = 0.00241578 s +E Equations = 0.00059 s +p Equations = 0.002158 s +calculate parcels = 4.84798 s +chemistry correctThermo = 0.002756 s +turbulence correct = 0.001051 s +combustion correct(in Y) = 0.0838982 s +percentage of chemistry = 88.8865 % +percentage of rho/U/Y/E = 4.58616 % +========Time details of each equation======= +rhoEqn Time = 0.000318 s +rhoEqn assamble = 0.000238 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001139 s +UEqn assamble = 0.000704 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000435 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001758 s +YEqn assamble = 0.000675 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000179 s +YEqn correct boundary = 0 s +EEqn Time = 0.000439 s +EEqn assamble = 0.000328 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 16.33 s ClockTime = 17 s +Courant Number mean: 0.000244097 max: 0.0162634 +Time = 0.00034 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 4623 + Current mass in system = 5.30106e-10 + Linear momentum = (2.43259e-11 -5.37508e-09 0) + |Linear momentum| = 5.37514e-09 + Linear kinetic energy = 2.85667e-08 + model1: + number of parcels added = 4623 + mass introduced = 5.34259e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.144, 520.12 + Mass transfer phase change = 4.15375e-12 + D10, D32, Dmax (mu) = 34.6691, 77.1704, 148.805 + Liquid penetration 95% mass (m) = 0.00279898 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00614989, Final residual = 7.47161e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0114339, Final residual = 2.9891e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00490559, Final residual = 4.32239e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00509443, Final residual = 2.48461e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00534078, Final residual = 2.41396e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00534081, Final residual = 2.41655e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00461994, Final residual = 3.07748e-07, No Iterations 1 +min/max(T) = 626.495, 820.974 +GAMG: Solving for p, Initial residual = 0.0347578, Final residual = 0.00035323, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.18926e-07, global = 8.9138e-07, cumulative = 9.58616e-05 +GAMG: Solving for p, Initial residual = 0.000342274, Final residual = 4.43126e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.82514e-07, global = 8.82464e-07, cumulative = 9.6744e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000756198, Final residual = 1.23294e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0066517, Final residual = 2.51182e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.093832 s +other Time = 0 s +rho Equations = 0.000129 s +U Equations = 0.000957 s +Y Equations = 0.00265329 s +E Equations = 0.000671 s +p Equations = 0.002598 s +calculate parcels = 4.93418 s +chemistry correctThermo = 0.002757 s +turbulence correct = 0.001276 s +combustion correct(in Y) = 0.0826147 s +percentage of chemistry = 88.0453 % +percentage of rho/U/Y/E = 4.7002 % +========Time details of each equation======= +rhoEqn Time = 0.000314 s +rhoEqn assamble = 0.000251 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000957 s +UEqn assamble = 0.000595 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000362 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002114 s +YEqn assamble = 0.000748 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000265 s +YEqn correct boundary = 0 s +EEqn Time = 0.000508 s +EEqn assamble = 0.000384 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000124 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 16.51 s ClockTime = 17 s +Courant Number mean: 0.000242911 max: 0.0163155 +Time = 0.0003425 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 4674 + Current mass in system = 5.34321e-10 + Linear momentum = (2.48316e-11 -5.41022e-09 0) + |Linear momentum| = 5.41027e-09 + Linear kinetic energy = 2.87106e-08 + model1: + number of parcels added = 4674 + mass introduced = 5.38552e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.13, 520.704 + Mass transfer phase change = 4.23077e-12 + D10, D32, Dmax (mu) = 34.7243, 77.24, 148.811 + Liquid penetration 95% mass (m) = 0.00282088 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00622486, Final residual = 7.86737e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0114172, Final residual = 3.01552e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00488909, Final residual = 4.31204e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00504544, Final residual = 2.45956e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00530069, Final residual = 2.38805e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00530072, Final residual = 2.39058e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00457267, Final residual = 3.02199e-07, No Iterations 1 +min/max(T) = 626.979, 821.25 +GAMG: Solving for p, Initial residual = 0.0337231, Final residual = 0.000308263, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.20459e-07, global = 8.96958e-07, cumulative = 9.7641e-05 +GAMG: Solving for p, Initial residual = 0.000299736, Final residual = 2.72057e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.87694e-07, global = 8.87663e-07, cumulative = 9.85287e-05 +smoothSolver: Solving for epsilon, Initial residual = 0.000761718, Final residual = 1.25107e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.006608, Final residual = 2.50868e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.097928 s +other Time = 0 s +rho Equations = 0.000167 s +U Equations = 0.001133 s +Y Equations = 0.00234912 s +E Equations = 0.000604 s +p Equations = 0.003617 s +calculate parcels = 5.02369 s +chemistry correctThermo = 0.004364 s +turbulence correct = 0.001774 s +combustion correct(in Y) = 0.0837019 s +percentage of chemistry = 85.4729 % +percentage of rho/U/Y/E = 4.34311 % +========Time details of each equation======= +rhoEqn Time = 0.000437 s +rhoEqn assamble = 0.000329 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000108 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001132 s +UEqn assamble = 0.000696 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000436 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001713 s +YEqn assamble = 0.000638 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00018 s +YEqn correct boundary = 0 s +EEqn Time = 0.000448 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 16.69 s ClockTime = 17 s +Courant Number mean: 0.000241718 max: 0.0163799 +Time = 0.000345 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 37 new parcels + +Cloud: sprayCloud + Current number of parcels = 4710 + Current mass in system = 5.37377e-10 + Linear momentum = (2.57965e-11 -5.4315e-09 0) + |Linear momentum| = 5.43156e-09 + Linear kinetic energy = 2.87715e-08 + model1: + number of parcels added = 4711 + mass introduced = 5.41686e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.151, 521.068 + Mass transfer phase change = 4.30881e-12 + D10, D32, Dmax (mu) = 38.4465, 77.2094, 148.816 + Liquid penetration 95% mass (m) = 0.00284329 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00641468, Final residual = 8.39162e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0113579, Final residual = 3.02532e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.004755, Final residual = 4.00619e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00501308, Final residual = 2.35808e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0052594, Final residual = 2.36546e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00525942, Final residual = 2.36796e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00450361, Final residual = 2.94427e-07, No Iterations 1 +min/max(T) = 627.433, 821.53 +GAMG: Solving for p, Initial residual = 0.0331541, Final residual = 0.000322778, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.31346e-07, global = 9.07112e-07, cumulative = 9.94358e-05 +GAMG: Solving for p, Initial residual = 0.000315264, Final residual = 3.23561e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.995e-07, global = 8.99466e-07, cumulative = 0.000100335 +smoothSolver: Solving for epsilon, Initial residual = 0.000766661, Final residual = 1.26872e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00656289, Final residual = 2.50504e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.090567 s +other Time = 1e-06 s +rho Equations = 0.00016 s +U Equations = 0.001147 s +Y Equations = 0.00238223 s +E Equations = 0.000604 s +p Equations = 0.002152 s +calculate parcels = 5.11276 s +chemistry correctThermo = 0.002767 s +turbulence correct = 0.00104 s +combustion correct(in Y) = 0.0801208 s +percentage of chemistry = 88.4657 % +percentage of rho/U/Y/E = 4.74039 % +========Time details of each equation======= +rhoEqn Time = 0.000298 s +rhoEqn assamble = 0.000234 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001146 s +UEqn assamble = 0.000702 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000444 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001732 s +YEqn assamble = 0.000639 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000182 s +YEqn correct boundary = 0 s +EEqn Time = 0.000447 s +EEqn assamble = 0.000333 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 16.87 s ClockTime = 17 s +Courant Number mean: 0.00024053 max: 0.0164457 +Time = 0.0003475 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 39 new parcels + +Cloud: sprayCloud + Current number of parcels = 4749 + Current mass in system = 5.40603e-10 + Linear momentum = (2.60398e-11 -5.45517e-09 0) + |Linear momentum| = 5.45523e-09 + Linear kinetic energy = 2.88484e-08 + model1: + number of parcels added = 4750 + mass introduced = 5.44989e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.15, 521.224 + Mass transfer phase change = 4.38643e-12 + D10, D32, Dmax (mu) = 38.504, 77.2101, 148.821 + Liquid penetration 95% mass (m) = 0.0028656 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00645044, Final residual = 8.91473e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0112696, Final residual = 2.98613e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00478682, Final residual = 4.11883e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00494101, Final residual = 2.38108e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00522177, Final residual = 2.35237e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0052218, Final residual = 2.35482e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00450207, Final residual = 3.05131e-07, No Iterations 1 +min/max(T) = 627.944, 821.813 +GAMG: Solving for p, Initial residual = 0.0326032, Final residual = 0.000328844, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.29539e-07, global = 8.99725e-07, cumulative = 0.000101235 +GAMG: Solving for p, Initial residual = 0.000320187, Final residual = 4.85804e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.94702e-07, global = 8.94652e-07, cumulative = 0.00010213 +smoothSolver: Solving for epsilon, Initial residual = 0.000771588, Final residual = 1.28506e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00652008, Final residual = 2.49941e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.08302 s +other Time = 0 s +rho Equations = 0.000163 s +U Equations = 0.001128 s +Y Equations = 0.00247345 s +E Equations = 0.000603 s +p Equations = 0.002218 s +calculate parcels = 5.19981 s +chemistry correctThermo = 0.002757 s +turbulence correct = 0.001085 s +combustion correct(in Y) = 0.0724035 s +percentage of chemistry = 87.2122 % +percentage of rho/U/Y/E = 5.26073 % +========Time details of each equation======= +rhoEqn Time = 0.000309 s +rhoEqn assamble = 0.000245 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001128 s +UEqn assamble = 0.000697 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000431 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001765 s +YEqn assamble = 0.000659 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00016 s +YEqn correct boundary = 0 s +EEqn Time = 0.000449 s +EEqn assamble = 0.000334 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 17.04 s ClockTime = 17 s +Courant Number mean: 0.000239207 max: 0.0164497 +Time = 0.00035 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 4800 + Current mass in system = 5.44849e-10 + Linear momentum = (2.58071e-11 -5.49151e-09 0) + |Linear momentum| = 5.49157e-09 + Linear kinetic energy = 2.90057e-08 + model1: + number of parcels added = 4801 + mass introduced = 5.49313e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.146, 521.184 + Mass transfer phase change = 4.46463e-12 + D10, D32, Dmax (mu) = 38.5735, 77.2387, 149.049 + Liquid penetration 95% mass (m) = 0.00288698 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00631519, Final residual = 8.63146e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0112123, Final residual = 3.00664e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0047826, Final residual = 4.18451e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00489988, Final residual = 2.36716e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00518091, Final residual = 2.3466e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00518094, Final residual = 2.349e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00448745, Final residual = 3.11259e-07, No Iterations 1 +min/max(T) = 627.709, 822.099 +GAMG: Solving for p, Initial residual = 0.0312422, Final residual = 0.000304412, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.35504e-07, global = 9.08813e-07, cumulative = 0.000103038 +GAMG: Solving for p, Initial residual = 0.000298654, Final residual = 5.46996e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.01438e-07, global = 9.01374e-07, cumulative = 0.00010394 +smoothSolver: Solving for epsilon, Initial residual = 0.000776007, Final residual = 1.2995e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00647654, Final residual = 2.48945e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.090595 s +other Time = 0 s +rho Equations = 0.000155 s +U Equations = 0.001186 s +Y Equations = 0.00306083 s +E Equations = 0.000777 s +p Equations = 0.002268 s +calculate parcels = 5.28851 s +chemistry correctThermo = 0.003779 s +turbulence correct = 0.001073 s +combustion correct(in Y) = 0.0780992 s +percentage of chemistry = 86.2069 % +percentage of rho/U/Y/E = 5.71647 % +========Time details of each equation======= +rhoEqn Time = 0.000302 s +rhoEqn assamble = 0.00024 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001185 s +UEqn assamble = 0.000745 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00044 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002414 s +YEqn assamble = 0.00092 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000361 s +YEqn correct boundary = 0 s +EEqn Time = 0.000551 s +EEqn assamble = 0.000409 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000142 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 17.22 s ClockTime = 18 s +Courant Number mean: 0.000237809 max: 0.0164641 +Time = 0.0003525 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 35 new parcels + +Cloud: sprayCloud + Current number of parcels = 4835 + Current mass in system = 5.47756e-10 + Linear momentum = (2.55063e-11 -5.51161e-09 0) + |Linear momentum| = 5.51167e-09 + Linear kinetic energy = 2.90636e-08 + model1: + number of parcels added = 4836 + mass introduced = 5.52299e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.133, 520.957 + Mass transfer phase change = 4.54331e-12 + D10, D32, Dmax (mu) = 38.6152, 77.2468, 148.832 + Liquid penetration 95% mass (m) = 0.00290929 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0063684, Final residual = 8.75459e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0119076, Final residual = 3.16318e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00477013, Final residual = 4.22864e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00485608, Final residual = 2.35589e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00514233, Final residual = 2.34231e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00514235, Final residual = 2.34469e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00445506, Final residual = 3.103e-07, No Iterations 1 +min/max(T) = 627.213, 822.387 +GAMG: Solving for p, Initial residual = 0.0304756, Final residual = 0.000257332, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.34674e-07, global = 9.1433e-07, cumulative = 0.000104854 +GAMG: Solving for p, Initial residual = 0.000250808, Final residual = 1.94558e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.06883e-07, global = 9.0686e-07, cumulative = 0.000105761 +smoothSolver: Solving for epsilon, Initial residual = 0.000781078, Final residual = 1.31304e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00643278, Final residual = 2.47719e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.08685 s +other Time = 1e-06 s +rho Equations = 0.000179 s +U Equations = 0.001165 s +Y Equations = 0.00229569 s +E Equations = 0.000532 s +p Equations = 0.001779 s +calculate parcels = 5.38041 s +chemistry correctThermo = 0.002013 s +turbulence correct = 0.000881 s +combustion correct(in Y) = 0.0778073 s +percentage of chemistry = 89.5882 % +percentage of rho/U/Y/E = 4.80332 % +========Time details of each equation======= +rhoEqn Time = 0.000295 s +rhoEqn assamble = 0.000234 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001164 s +UEqn assamble = 0.000723 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000441 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001519 s +YEqn assamble = 0.000607 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 5.8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000393 s +EEqn assamble = 0.000291 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000102 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 17.4 s ClockTime = 18 s +Courant Number mean: 0.000236361 max: 0.0164862 +Time = 0.000355 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 4885 + Current mass in system = 5.51938e-10 + Linear momentum = (2.46932e-11 -5.54779e-09 0) + |Linear momentum| = 5.54784e-09 + Linear kinetic energy = 2.92244e-08 + model1: + number of parcels added = 4886 + mass introduced = 5.56561e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.142, 520.543 + Mass transfer phase change = 4.62256e-12 + D10, D32, Dmax (mu) = 38.6705, 77.3567, 148.837 + Liquid penetration 95% mass (m) = 0.00293087 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00633915, Final residual = 8.94798e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.012758, Final residual = 3.36344e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00471697, Final residual = 4.2004e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00481466, Final residual = 2.32233e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00510286, Final residual = 2.34609e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00510289, Final residual = 2.3485e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00441823, Final residual = 3.10643e-07, No Iterations 1 +min/max(T) = 626.772, 822.68 +GAMG: Solving for p, Initial residual = 0.0298987, Final residual = 0.00028481, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.46806e-07, global = 9.19788e-07, cumulative = 0.000106681 +GAMG: Solving for p, Initial residual = 0.000278041, Final residual = 2.50166e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.13421e-07, global = 9.1339e-07, cumulative = 0.000107594 +smoothSolver: Solving for epsilon, Initial residual = 0.000787343, Final residual = 1.32586e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00639024, Final residual = 2.46372e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.087747 s +other Time = 0 s +rho Equations = 0.000162 s +U Equations = 0.00115 s +Y Equations = 0.00234474 s +E Equations = 0.000602 s +p Equations = 0.002199 s +calculate parcels = 5.47214 s +chemistry correctThermo = 0.002786 s +turbulence correct = 0.001101 s +combustion correct(in Y) = 0.0772063 s +percentage of chemistry = 87.9874 % +percentage of rho/U/Y/E = 4.85343 % +========Time details of each equation======= +rhoEqn Time = 0.000305 s +rhoEqn assamble = 0.000241 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00115 s +UEqn assamble = 0.000704 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000446 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001697 s +YEqn assamble = 0.000632 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000179 s +YEqn correct boundary = 0 s +EEqn Time = 0.000446 s +EEqn assamble = 0.000334 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 17.58 s ClockTime = 18 s +Courant Number mean: 0.00023485 max: 0.0165085 +Time = 0.0003575 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 4933 + Current mass in system = 5.55973e-10 + Linear momentum = (2.55573e-11 -5.58235e-09 0) + |Linear momentum| = 5.58241e-09 + Linear kinetic energy = 2.93766e-08 + model1: + number of parcels added = 4934 + mass introduced = 5.60675e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.143, 519.942 + Mass transfer phase change = 4.70243e-12 + D10, D32, Dmax (mu) = 38.7297, 77.3731, 148.842 + Liquid penetration 95% mass (m) = 0.00295289 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00624611, Final residual = 8.73813e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0136694, Final residual = 3.59637e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00469433, Final residual = 4.22231e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00477361, Final residual = 2.32286e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00506083, Final residual = 2.35292e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00506086, Final residual = 2.35532e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00438555, Final residual = 3.09946e-07, No Iterations 1 +min/max(T) = 626.373, 822.977 +GAMG: Solving for p, Initial residual = 0.0290921, Final residual = 0.000252247, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.4901e-07, global = 9.27256e-07, cumulative = 0.000108521 +GAMG: Solving for p, Initial residual = 0.000246132, Final residual = 2.73965e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.20674e-07, global = 9.20641e-07, cumulative = 0.000109442 +smoothSolver: Solving for epsilon, Initial residual = 0.000793249, Final residual = 1.33694e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00634692, Final residual = 2.44669e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.094289 s +other Time = 0 s +rho Equations = 0.00015 s +U Equations = 0.001116 s +Y Equations = 0.00256408 s +E Equations = 0.000622 s +p Equations = 0.002572 s +calculate parcels = 5.56099 s +chemistry correctThermo = 0.002806 s +turbulence correct = 0.001221 s +combustion correct(in Y) = 0.0830319 s +percentage of chemistry = 88.0611 % +percentage of rho/U/Y/E = 4.72174 % +========Time details of each equation======= +rhoEqn Time = 0.000322 s +rhoEqn assamble = 0.000254 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001116 s +UEqn assamble = 0.000688 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000428 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001865 s +YEqn assamble = 0.00072 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00016 s +YEqn correct boundary = 0 s +EEqn Time = 0.000462 s +EEqn assamble = 0.000349 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 17.77 s ClockTime = 18 s +Courant Number mean: 0.00023337 max: 0.016533 +Time = 0.00036 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 4984 + Current mass in system = 5.60285e-10 + Linear momentum = (2.64476e-11 -5.62054e-09 0) + |Linear momentum| = 5.62061e-09 + Linear kinetic energy = 2.95546e-08 + model1: + number of parcels added = 4985 + mass introduced = 5.65068e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.145, 520.875 + Mass transfer phase change = 4.78282e-12 + D10, D32, Dmax (mu) = 38.788, 77.4154, 148.847 + Liquid penetration 95% mass (m) = 0.00297467 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00612933, Final residual = 8.69578e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0145152, Final residual = 3.78025e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00450552, Final residual = 3.85631e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00473018, Final residual = 2.1378e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00502278, Final residual = 2.35402e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0050228, Final residual = 2.35642e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00431989, Final residual = 3.00895e-07, No Iterations 1 +min/max(T) = 626.011, 823.276 +GAMG: Solving for p, Initial residual = 0.0289055, Final residual = 0.000272143, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.55783e-07, global = 9.35437e-07, cumulative = 0.000110377 +GAMG: Solving for p, Initial residual = 0.000265892, Final residual = 2.11161e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.26616e-07, global = 9.26591e-07, cumulative = 0.000111304 +smoothSolver: Solving for epsilon, Initial residual = 0.00079882, Final residual = 1.34726e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00630249, Final residual = 2.42849e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.066817 s +other Time = 0 s +rho Equations = 0.000152 s +U Equations = 0.001043 s +Y Equations = 0.00218373 s +E Equations = 0.000506 s +p Equations = 0.001914 s +calculate parcels = 5.64405 s +chemistry correctThermo = 0.001977 s +turbulence correct = 0.000932 s +combustion correct(in Y) = 0.0579273 s +percentage of chemistry = 86.6954 % +percentage of rho/U/Y/E = 5.81399 % +========Time details of each equation======= +rhoEqn Time = 0.000277 s +rhoEqn assamble = 0.000222 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001043 s +UEqn assamble = 0.00066 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000383 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001578 s +YEqn assamble = 0.000593 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000131 s +YEqn correct boundary = 0 s +EEqn Time = 0.000379 s +EEqn assamble = 0.000285 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 17.92 s ClockTime = 18 s +Courant Number mean: 0.000232027 max: 0.0165805 +Time = 0.0003625 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 37 new parcels + +Cloud: sprayCloud + Current number of parcels = 5021 + Current mass in system = 5.63411e-10 + Linear momentum = (2.65106e-11 -5.64411e-09 0) + |Linear momentum| = 5.64417e-09 + Linear kinetic energy = 2.96405e-08 + model1: + number of parcels added = 5022 + mass introduced = 5.68275e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.143, 521.242 + Mass transfer phase change = 4.86353e-12 + D10, D32, Dmax (mu) = 38.8202, 77.4375, 148.853 + Liquid penetration 95% mass (m) = 0.00299634 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00631871, Final residual = 8.91018e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0153575, Final residual = 3.93789e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00449301, Final residual = 3.734e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00467917, Final residual = 2.10715e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00498097, Final residual = 2.35547e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.004981, Final residual = 2.35786e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00428069, Final residual = 2.92355e-07, No Iterations 1 +min/max(T) = 625.692, 823.579 +GAMG: Solving for p, Initial residual = 0.0281901, Final residual = 0.000255384, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.61356e-07, global = 9.36956e-07, cumulative = 0.000112241 +GAMG: Solving for p, Initial residual = 0.000248999, Final residual = 4.32443e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.30294e-07, global = 9.30239e-07, cumulative = 0.000113171 +smoothSolver: Solving for epsilon, Initial residual = 0.000804433, Final residual = 1.35731e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00625896, Final residual = 2.41021e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.067735 s +other Time = 0 s +rho Equations = 0.000156 s +U Equations = 0.001033 s +Y Equations = 0.00230888 s +E Equations = 0.00051 s +p Equations = 0.00229 s +calculate parcels = 5.71424 s +chemistry correctThermo = 0.001926 s +turbulence correct = 0.000893 s +combustion correct(in Y) = 0.0584401 s +percentage of chemistry = 86.2776 % +percentage of rho/U/Y/E = 5.917 % +========Time details of each equation======= +rhoEqn Time = 0.000287 s +rhoEqn assamble = 0.000224 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001031 s +UEqn assamble = 0.000657 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000374 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001556 s +YEqn assamble = 0.000562 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.3e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000385 s +EEqn assamble = 0.00029 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 18.05 s ClockTime = 18 s +Courant Number mean: 0.000230806 max: 0.0166268 +Time = 0.000365 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 5072 + Current mass in system = 5.67749e-10 + Linear momentum = (2.67548e-11 -5.68328e-09 0) + |Linear momentum| = 5.68335e-09 + Linear kinetic energy = 2.98278e-08 + model1: + number of parcels added = 5073 + mass introduced = 5.72694e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.137, 519.694 + Mass transfer phase change = 4.9446e-12 + D10, D32, Dmax (mu) = 38.8802, 77.5266, 148.858 + Liquid penetration 95% mass (m) = 0.00301812 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00628704, Final residual = 8.89575e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0162238, Final residual = 4.13745e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00461885, Final residual = 3.6471e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00466621, Final residual = 2.16558e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00494417, Final residual = 2.35286e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00494419, Final residual = 2.35524e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00424544, Final residual = 2.872e-07, No Iterations 1 +min/max(T) = 625.395, 823.887 +GAMG: Solving for p, Initial residual = 0.0279687, Final residual = 0.000226959, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.60575e-07, global = 9.38661e-07, cumulative = 0.00011411 +GAMG: Solving for p, Initial residual = 0.000221787, Final residual = 3.02808e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.34368e-07, global = 9.34329e-07, cumulative = 0.000115044 +smoothSolver: Solving for epsilon, Initial residual = 0.0008099, Final residual = 1.36639e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.006216, Final residual = 2.39056e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.093929 s +other Time = 1e-06 s +rho Equations = 0.000166 s +U Equations = 0.001732 s +Y Equations = 0.00257178 s +E Equations = 0.000603 s +p Equations = 0.002407 s +calculate parcels = 5.78456 s +chemistry correctThermo = 0.002787 s +turbulence correct = 0.001096 s +combustion correct(in Y) = 0.0823752 s +percentage of chemistry = 87.6995 % +percentage of rho/U/Y/E = 5.40066 % +========Time details of each equation======= +rhoEqn Time = 0.000325 s +rhoEqn assamble = 0.000261 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001731 s +UEqn assamble = 0.000985 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000746 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001731 s +YEqn assamble = 0.000659 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000447 s +EEqn assamble = 0.000334 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 18.22 s ClockTime = 19 s +Courant Number mean: 0.000229574 max: 0.0166707 +Time = 0.0003675 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 5116 + Current mass in system = 5.71503e-10 + Linear momentum = (2.65013e-11 -5.71535e-09 0) + |Linear momentum| = 5.71541e-09 + Linear kinetic energy = 2.99709e-08 + model1: + number of parcels added = 5117 + mass introduced = 5.76529e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.15, 518.122 + Mass transfer phase change = 5.02603e-12 + D10, D32, Dmax (mu) = 38.9315, 77.5764, 148.863 + Liquid penetration 95% mass (m) = 0.00304087 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00608111, Final residual = 8.98888e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0170104, Final residual = 4.33428e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00455554, Final residual = 3.65889e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00461829, Final residual = 2.14659e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00490467, Final residual = 2.35231e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00490469, Final residual = 2.35467e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00420165, Final residual = 2.84028e-07, No Iterations 1 +min/max(T) = 625.175, 824.199 +GAMG: Solving for p, Initial residual = 0.028006, Final residual = 0.000258094, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.6948e-07, global = 9.47358e-07, cumulative = 0.000115992 +GAMG: Solving for p, Initial residual = 0.000252279, Final residual = 2.60436e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.38608e-07, global = 9.38574e-07, cumulative = 0.00011693 +smoothSolver: Solving for epsilon, Initial residual = 0.000815412, Final residual = 1.37572e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00617546, Final residual = 2.37288e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.094258 s +other Time = 0 s +rho Equations = 0.000157 s +U Equations = 0.001132 s +Y Equations = 0.00243507 s +E Equations = 0.000653 s +p Equations = 0.002171 s +calculate parcels = 5.87612 s +chemistry correctThermo = 0.002774 s +turbulence correct = 0.001086 s +combustion correct(in Y) = 0.0836559 s +percentage of chemistry = 88.7521 % +percentage of rho/U/Y/E = 4.64372 % +========Time details of each equation======= +rhoEqn Time = 0.000301 s +rhoEqn assamble = 0.000237 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001131 s +UEqn assamble = 0.000703 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000428 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001803 s +YEqn assamble = 0.000673 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00022 s +YEqn correct boundary = 0 s +EEqn Time = 0.000497 s +EEqn assamble = 0.000375 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000122 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 18.4 s ClockTime = 19 s +Courant Number mean: 0.000228301 max: 0.0167063 +Time = 0.00037 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 5167 + Current mass in system = 5.7588e-10 + Linear momentum = (2.65106e-11 -5.75562e-09 0) + |Linear momentum| = 5.75569e-09 + Linear kinetic energy = 3.01689e-08 + model1: + number of parcels added = 5168 + mass introduced = 5.80988e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.144, 516.542 + Mass transfer phase change = 5.10802e-12 + D10, D32, Dmax (mu) = 38.9859, 77.6166, 148.869 + Liquid penetration 95% mass (m) = 0.00306205 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00572009, Final residual = 8.43619e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0177238, Final residual = 4.52328e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00448422, Final residual = 3.63702e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00456768, Final residual = 2.1067e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0048666, Final residual = 2.34938e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00486662, Final residual = 2.35172e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00414682, Final residual = 2.81164e-07, No Iterations 1 +min/max(T) = 625.013, 824.513 +GAMG: Solving for p, Initial residual = 0.028141, Final residual = 0.000339232, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.82902e-07, global = 9.5397e-07, cumulative = 0.000117884 +GAMG: Solving for p, Initial residual = 0.00033754, Final residual = 4.54979e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.45052e-07, global = 9.45004e-07, cumulative = 0.000118829 +smoothSolver: Solving for epsilon, Initial residual = 0.000819776, Final residual = 1.38232e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00613285, Final residual = 9.96818e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.088404 s +other Time = 1e-06 s +rho Equations = 0.000186 s +U Equations = 0.00113 s +Y Equations = 0.00247932 s +E Equations = 0.000506 s +p Equations = 0.001948 s +calculate parcels = 5.97354 s +chemistry correctThermo = 0.002627 s +turbulence correct = 0.000823 s +combustion correct(in Y) = 0.0784987 s +percentage of chemistry = 88.7954 % +percentage of rho/U/Y/E = 4.86552 % +========Time details of each equation======= +rhoEqn Time = 0.000309 s +rhoEqn assamble = 0.000234 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00113 s +UEqn assamble = 0.000694 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000436 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001829 s +YEqn assamble = 0.000685 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000224 s +YEqn correct boundary = 0 s +EEqn Time = 0.000387 s +EEqn assamble = 0.000287 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.0001 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 18.59 s ClockTime = 19 s +Courant Number mean: 0.000227074 max: 0.0167042 +Time = 0.0003725 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 55 new parcels + +Cloud: sprayCloud + Current number of parcels = 5222 + Current mass in system = 5.80635e-10 + Linear momentum = (2.56275e-11 -5.80104e-09 0) + |Linear momentum| = 5.8011e-09 + Linear kinetic energy = 3.0403e-08 + model1: + number of parcels added = 5223 + mass introduced = 5.85825e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.147, 514.969 + Mass transfer phase change = 5.19059e-12 + D10, D32, Dmax (mu) = 39.0101, 77.6646, 148.874 + Liquid penetration 95% mass (m) = 0.00308434 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00556955, Final residual = 8.42019e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0181714, Final residual = 4.60488e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00442854, Final residual = 3.67492e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00452459, Final residual = 2.08058e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00483045, Final residual = 2.34374e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00483047, Final residual = 2.34607e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00410541, Final residual = 2.82174e-07, No Iterations 1 +min/max(T) = 624.893, 824.828 +GAMG: Solving for p, Initial residual = 0.0276403, Final residual = 0.000300248, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.83328e-07, global = 9.6423e-07, cumulative = 0.000119793 +GAMG: Solving for p, Initial residual = 0.000294658, Final residual = 3.85975e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.51759e-07, global = 9.51721e-07, cumulative = 0.000120745 +smoothSolver: Solving for epsilon, Initial residual = 0.000823809, Final residual = 1.38783e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00608939, Final residual = 9.88707e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.081031 s +other Time = 0 s +rho Equations = 0.000158 s +U Equations = 0.001134 s +Y Equations = 0.0021114 s +E Equations = 0.000509 s +p Equations = 0.00186 s +calculate parcels = 6.06243 s +chemistry correctThermo = 0.001974 s +turbulence correct = 0.000864 s +combustion correct(in Y) = 0.0722376 s +percentage of chemistry = 89.1481 % +percentage of rho/U/Y/E = 4.82827 % +========Time details of each equation======= +rhoEqn Time = 0.000281 s +rhoEqn assamble = 0.000225 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001134 s +UEqn assamble = 0.000702 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000432 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001459 s +YEqn assamble = 0.000553 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000388 s +EEqn assamble = 0.000274 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 18.76 s ClockTime = 19 s +Courant Number mean: 0.000225896 max: 0.0166998 +Time = 0.000375 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 61 new parcels + +Cloud: sprayCloud + Current number of parcels = 5283 + Current mass in system = 5.85958e-10 + Linear momentum = (2.60621e-11 -5.85396e-09 0) + |Linear momentum| = 5.85402e-09 + Linear kinetic energy = 3.06877e-08 + model1: + number of parcels added = 5284 + mass introduced = 5.91232e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.14, 513.41 + Mass transfer phase change = 5.27385e-12 + D10, D32, Dmax (mu) = 39.0657, 77.7194, 148.879 + Liquid penetration 95% mass (m) = 0.00310554 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00605736, Final residual = 9.33956e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0186017, Final residual = 4.68225e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00438785, Final residual = 3.6629e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00447539, Final residual = 2.06094e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00479229, Final residual = 2.33618e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00479231, Final residual = 2.33849e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00403946, Final residual = 2.83961e-07, No Iterations 1 +min/max(T) = 624.806, 825.147 +GAMG: Solving for p, Initial residual = 0.0275759, Final residual = 0.000323928, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.96018e-07, global = 9.744e-07, cumulative = 0.00012172 +GAMG: Solving for p, Initial residual = 0.000321851, Final residual = 4.41395e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.59779e-07, global = 9.59731e-07, cumulative = 0.000122679 +smoothSolver: Solving for epsilon, Initial residual = 0.000827079, Final residual = 1.39168e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00604497, Final residual = 9.80251e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094219 s +other Time = 1e-06 s +rho Equations = 0.000165 s +U Equations = 0.001129 s +Y Equations = 0.00241788 s +E Equations = 0.000616 s +p Equations = 0.002379 s +calculate parcels = 6.15648 s +chemistry correctThermo = 0.002885 s +turbulence correct = 0.001006 s +combustion correct(in Y) = 0.0834071 s +percentage of chemistry = 88.5247 % +percentage of rho/U/Y/E = 4.59343 % +========Time details of each equation======= +rhoEqn Time = 0.000321 s +rhoEqn assamble = 0.000253 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001128 s +UEqn assamble = 0.000692 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000436 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001763 s +YEqn assamble = 0.000647 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000182 s +YEqn correct boundary = 0 s +EEqn Time = 0.000459 s +EEqn assamble = 0.000343 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 18.95 s ClockTime = 19 s +Courant Number mean: 0.000224842 max: 0.0166945 +Time = 0.0003775 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 42 new parcels + +Cloud: sprayCloud + Current number of parcels = 5325 + Current mass in system = 5.89626e-10 + Linear momentum = (2.51352e-11 -5.88556e-09 0) + |Linear momentum| = 5.88562e-09 + Linear kinetic energy = 3.0833e-08 + model1: + number of parcels added = 5326 + mass introduced = 5.94983e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.154, 511.876 + Mass transfer phase change = 5.35762e-12 + D10, D32, Dmax (mu) = 39.1202, 77.7533, 148.885 + Liquid penetration 95% mass (m) = 0.00312566 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00700134, Final residual = 1.92079e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0189585, Final residual = 4.72257e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00435525, Final residual = 3.65502e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00443615, Final residual = 2.04924e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0047568, Final residual = 2.32564e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00475683, Final residual = 2.32793e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00400046, Final residual = 2.82154e-07, No Iterations 1 +min/max(T) = 624.769, 825.465 +GAMG: Solving for p, Initial residual = 0.0279729, Final residual = 0.000310652, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.99938e-07, global = 9.73079e-07, cumulative = 0.000123652 +GAMG: Solving for p, Initial residual = 0.000308623, Final residual = 5.74288e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.6559e-07, global = 9.65521e-07, cumulative = 0.000124618 +smoothSolver: Solving for epsilon, Initial residual = 0.000831215, Final residual = 1.39711e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00600322, Final residual = 9.7252e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095819 s +other Time = 1e-06 s +rho Equations = 0.000161 s +U Equations = 0.001187 s +Y Equations = 0.00237864 s +E Equations = 0.000634 s +p Equations = 0.002214 s +calculate parcels = 6.2567 s +chemistry correctThermo = 0.002782 s +turbulence correct = 0.001593 s +combustion correct(in Y) = 0.0846674 s +percentage of chemistry = 88.3618 % +percentage of rho/U/Y/E = 4.55092 % +========Time details of each equation======= +rhoEqn Time = 0.000305 s +rhoEqn assamble = 0.000243 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001187 s +UEqn assamble = 0.000685 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000502 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001685 s +YEqn assamble = 0.000648 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000142 s +YEqn correct boundary = 0 s +EEqn Time = 0.000477 s +EEqn assamble = 0.000357 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00012 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 19.14 s ClockTime = 20 s +Courant Number mean: 0.00022378 max: 0.0167162 +Time = 0.00038 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 5375 + Current mass in system = 5.93994e-10 + Linear momentum = (2.58331e-11 -5.92625e-09 0) + |Linear momentum| = 5.9263e-09 + Linear kinetic energy = 3.10378e-08 + model1: + number of parcels added = 5376 + mass introduced = 5.99436e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.145, 510.372 + Mass transfer phase change = 5.442e-12 + D10, D32, Dmax (mu) = 39.1306, 77.7399, 148.89 + Liquid penetration 95% mass (m) = 0.00314664 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00716614, Final residual = 1.99234e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0192966, Final residual = 4.78555e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0043127, Final residual = 3.63894e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00439732, Final residual = 2.02444e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00472207, Final residual = 2.31345e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00472209, Final residual = 2.31572e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0039408, Final residual = 2.81568e-07, No Iterations 1 +min/max(T) = 624.766, 825.792 +GAMG: Solving for p, Initial residual = 0.0280799, Final residual = 0.000282349, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.0044e-06, global = 9.77346e-07, cumulative = 0.000125595 +GAMG: Solving for p, Initial residual = 0.000279595, Final residual = 3.18926e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.7253e-07, global = 9.72491e-07, cumulative = 0.000126568 +smoothSolver: Solving for epsilon, Initial residual = 0.000834919, Final residual = 1.40145e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00596074, Final residual = 9.64546e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.091379 s +other Time = 0 s +rho Equations = 0.000169 s +U Equations = 0.00126 s +Y Equations = 0.00247181 s +E Equations = 0.000648 s +p Equations = 0.002391 s +calculate parcels = 6.35892 s +chemistry correctThermo = 0.002792 s +turbulence correct = 0.001107 s +combustion correct(in Y) = 0.0803392 s +percentage of chemistry = 87.9187 % +percentage of rho/U/Y/E = 4.97796 % +========Time details of each equation======= +rhoEqn Time = 0.000324 s +rhoEqn assamble = 0.000257 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001259 s +UEqn assamble = 0.000749 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00051 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00182 s +YEqn assamble = 0.000679 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000185 s +YEqn correct boundary = 0 s +EEqn Time = 0.000481 s +EEqn assamble = 0.000362 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000119 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 19.34 s ClockTime = 20 s +Courant Number mean: 0.000222765 max: 0.0167391 +Time = 0.0003825 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 40 new parcels + +Cloud: sprayCloud + Current number of parcels = 5414 + Current mass in system = 5.97472e-10 + Linear momentum = (2.62841e-11 -5.95525e-09 0) + |Linear momentum| = 5.95531e-09 + Linear kinetic energy = 3.11662e-08 + model1: + number of parcels added = 5416 + mass introduced = 6.03e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.144, 508.954 + Mass transfer phase change = 5.52757e-12 + D10, D32, Dmax (mu) = 44.1515, 77.7696, 148.895 + Liquid penetration 95% mass (m) = 0.00316733 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00721661, Final residual = 2.03836e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0193729, Final residual = 4.80996e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00429005, Final residual = 3.66377e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00437675, Final residual = 2.05705e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00468579, Final residual = 2.29903e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00468582, Final residual = 2.30138e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00389755, Final residual = 2.75379e-07, No Iterations 1 +min/max(T) = 624.77, 826.12 +GAMG: Solving for p, Initial residual = 0.027869, Final residual = 0.000292174, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.01899e-06, global = 9.92944e-07, cumulative = 0.000127561 +GAMG: Solving for p, Initial residual = 0.00029119, Final residual = 4.35856e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.86367e-07, global = 9.86314e-07, cumulative = 0.000128547 +smoothSolver: Solving for epsilon, Initial residual = 0.000839013, Final residual = 1.40647e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00591964, Final residual = 9.5689e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.089033 s +other Time = 1e-06 s +rho Equations = 0.000158 s +U Equations = 0.001174 s +Y Equations = 0.00202367 s +E Equations = 0.000499 s +p Equations = 0.001772 s +calculate parcels = 6.45915 s +chemistry correctThermo = 0.001956 s +turbulence correct = 0.000853 s +combustion correct(in Y) = 0.0803953 s +percentage of chemistry = 90.2984 % +percentage of rho/U/Y/E = 4.32948 % +========Time details of each equation======= +rhoEqn Time = 0.000276 s +rhoEqn assamble = 0.000218 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001174 s +UEqn assamble = 0.000667 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000507 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001373 s +YEqn assamble = 0.000531 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.0001 s +YEqn correct boundary = 0 s +EEqn Time = 0.000381 s +EEqn assamble = 0.000284 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.7e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 19.53 s ClockTime = 20 s +Courant Number mean: 0.000221721 max: 0.0167676 +Time = 0.000385 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 47 new parcels + +Cloud: sprayCloud + Current number of parcels = 5461 + Current mass in system = 6.01558e-10 + Linear momentum = (2.61506e-11 -5.99215e-09 0) + |Linear momentum| = 5.99221e-09 + Linear kinetic energy = 3.1346e-08 + model1: + number of parcels added = 5463 + mass introduced = 6.07171e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.14, 507.688 + Mass transfer phase change = 5.61299e-12 + D10, D32, Dmax (mu) = 44.0008, 77.745, 148.901 + Liquid penetration 95% mass (m) = 0.0031877 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00720194, Final residual = 2.16553e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0193345, Final residual = 4.80221e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00433546, Final residual = 3.89607e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00432095, Final residual = 2.01171e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0046543, Final residual = 2.29593e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00465432, Final residual = 2.29827e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00385807, Final residual = 2.8121e-07, No Iterations 1 +min/max(T) = 624.806, 826.452 +GAMG: Solving for p, Initial residual = 0.0282609, Final residual = 0.000327318, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.02033e-06, global = 9.91575e-07, cumulative = 0.000129539 +GAMG: Solving for p, Initial residual = 0.00032698, Final residual = 3.97946e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.84621e-07, global = 9.84576e-07, cumulative = 0.000130523 +smoothSolver: Solving for epsilon, Initial residual = 0.000842834, Final residual = 1.41026e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00588021, Final residual = 9.49432e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094247 s +other Time = 0 s +rho Equations = 0.000165 s +U Equations = 0.001332 s +Y Equations = 0.00238837 s +E Equations = 0.000615 s +p Equations = 0.002258 s +calculate parcels = 6.55056 s +chemistry correctThermo = 0.002771 s +turbulence correct = 0.001009 s +combustion correct(in Y) = 0.0835166 s +percentage of chemistry = 88.6146 % +percentage of rho/U/Y/E = 4.77508 % +========Time details of each equation======= +rhoEqn Time = 0.000309 s +rhoEqn assamble = 0.000241 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001331 s +UEqn assamble = 0.000787 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000544 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001743 s +YEqn assamble = 0.000664 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000183 s +YEqn correct boundary = 0 s +EEqn Time = 0.000459 s +EEqn assamble = 0.000344 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 19.71 s ClockTime = 20 s +Courant Number mean: 0.000220661 max: 0.0167573 +Time = 0.0003875 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 5510 + Current mass in system = 6.05817e-10 + Linear momentum = (2.63663e-11 -6.03128e-09 0) + |Linear momentum| = 6.03133e-09 + Linear kinetic energy = 3.15395e-08 + model1: + number of parcels added = 5512 + mass introduced = 6.11516e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.151, 507.054 + Mass transfer phase change = 5.69935e-12 + D10, D32, Dmax (mu) = 43.8141, 77.669, 148.906 + Liquid penetration 95% mass (m) = 0.00320767 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00684325, Final residual = 1.90743e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0190397, Final residual = 4.78215e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00426476, Final residual = 3.79075e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00429431, Final residual = 2.00537e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0046222, Final residual = 2.28561e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00462222, Final residual = 2.28793e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00378398, Final residual = 2.8049e-07, No Iterations 1 +min/max(T) = 624.897, 826.782 +GAMG: Solving for p, Initial residual = 0.0282604, Final residual = 0.0003546, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.03161e-06, global = 1.00691e-06, cumulative = 0.00013153 +GAMG: Solving for p, Initial residual = 0.000355179, Final residual = 6.96196e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.95471e-07, global = 9.95401e-07, cumulative = 0.000132525 +smoothSolver: Solving for epsilon, Initial residual = 0.000845568, Final residual = 1.41268e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.005839, Final residual = 9.41573e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095222 s +other Time = 0 s +rho Equations = 0.000162 s +U Equations = 0.00126 s +Y Equations = 0.00248129 s +E Equations = 0.000612 s +p Equations = 0.002341 s +calculate parcels = 6.62852 s +chemistry correctThermo = 0.002761 s +turbulence correct = 0.000886 s +combustion correct(in Y) = 0.0845207 s +percentage of chemistry = 88.7617 % +percentage of rho/U/Y/E = 4.74185 % +========Time details of each equation======= +rhoEqn Time = 0.000342 s +rhoEqn assamble = 0.000273 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00126 s +UEqn assamble = 0.000735 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000525 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001746 s +YEqn assamble = 0.000687 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000161 s +YEqn correct boundary = 0 s +EEqn Time = 0.000458 s +EEqn assamble = 0.000345 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 19.89 s ClockTime = 20 s +Courant Number mean: 0.000219674 max: 0.0167906 +Time = 0.00039 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 5558 + Current mass in system = 6.09987e-10 + Linear momentum = (2.71573e-11 -6.06917e-09 0) + |Linear momentum| = 6.06923e-09 + Linear kinetic energy = 3.17254e-08 + model1: + number of parcels added = 5560 + mass introduced = 6.15773e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.146, 507.16 + Mass transfer phase change = 5.78638e-12 + D10, D32, Dmax (mu) = 43.8976, 77.7019, 148.911 + Liquid penetration 95% mass (m) = 0.00322793 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00719493, Final residual = 1.97543e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.018609, Final residual = 4.66032e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0042333, Final residual = 3.80167e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00426138, Final residual = 2.00891e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00459036, Final residual = 2.27579e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00459038, Final residual = 2.2781e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00374199, Final residual = 2.77376e-07, No Iterations 1 +min/max(T) = 625.008, 827.113 +GAMG: Solving for p, Initial residual = 0.0291266, Final residual = 0.000348506, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.03856e-06, global = 1.01254e-06, cumulative = 0.000133538 +GAMG: Solving for p, Initial residual = 0.000347155, Final residual = 6.36058e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.00317e-06, global = 1.0031e-06, cumulative = 0.000134541 +smoothSolver: Solving for epsilon, Initial residual = 0.000849239, Final residual = 1.41666e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00580006, Final residual = 9.34439e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.082711 s +other Time = 0 s +rho Equations = 0.000135 s +U Equations = 0.00101 s +Y Equations = 0.00238355 s +E Equations = 0.00062 s +p Equations = 0.002197 s +calculate parcels = 6.72432 s +chemistry correctThermo = 0.002738 s +turbulence correct = 0.000993 s +combustion correct(in Y) = 0.0724675 s +percentage of chemistry = 87.6153 % +percentage of rho/U/Y/E = 5.01571 % +========Time details of each equation======= +rhoEqn Time = 0.000284 s +rhoEqn assamble = 0.000227 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00101 s +UEqn assamble = 0.000572 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000438 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001813 s +YEqn assamble = 0.000651 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000257 s +YEqn correct boundary = 0 s +EEqn Time = 0.000467 s +EEqn assamble = 0.000339 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000128 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 20.07 s ClockTime = 20 s +Courant Number mean: 0.000218595 max: 0.0168013 +Time = 0.0003925 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 5602 + Current mass in system = 6.138e-10 + Linear momentum = (2.81633e-11 -6.10233e-09 0) + |Linear momentum| = 6.10239e-09 + Linear kinetic energy = 3.18805e-08 + model1: + number of parcels added = 5604 + mass introduced = 6.19674e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.159, 507.28 + Mass transfer phase change = 5.87412e-12 + D10, D32, Dmax (mu) = 43.9639, 77.7329, 148.916 + Liquid penetration 95% mass (m) = 0.00324862 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00698784, Final residual = 2.05313e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0182039, Final residual = 4.54414e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00419385, Final residual = 3.76694e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00423117, Final residual = 2.01376e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00456045, Final residual = 2.26473e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00456047, Final residual = 2.26704e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00369495, Final residual = 2.76181e-07, No Iterations 1 +min/max(T) = 625.148, 827.45 +GAMG: Solving for p, Initial residual = 0.0294822, Final residual = 0.000306158, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.04499e-06, global = 1.01906e-06, cumulative = 0.00013556 +GAMG: Solving for p, Initial residual = 0.000302153, Final residual = 5.2266e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.0113e-06, global = 1.01124e-06, cumulative = 0.000136571 +smoothSolver: Solving for epsilon, Initial residual = 0.000853237, Final residual = 1.42112e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00576269, Final residual = 9.27812e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.078219 s +other Time = 1e-06 s +rho Equations = 0.0002 s +U Equations = 0.00133 s +Y Equations = 0.00217092 s +E Equations = 0.000559 s +p Equations = 0.002088 s +calculate parcels = 6.82935 s +chemistry correctThermo = 0.001985 s +turbulence correct = 0.000911 s +combustion correct(in Y) = 0.0687621 s +percentage of chemistry = 87.9097 % +percentage of rho/U/Y/E = 5.44615 % +========Time details of each equation======= +rhoEqn Time = 0.000396 s +rhoEqn assamble = 0.000305 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001329 s +UEqn assamble = 0.000798 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000531 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001473 s +YEqn assamble = 0.000571 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 7.9e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000416 s +EEqn assamble = 0.000314 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000102 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 20.25 s ClockTime = 21 s +Courant Number mean: 0.000217436 max: 0.0168233 +Time = 0.000395 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 47 new parcels + +Cloud: sprayCloud + Current number of parcels = 5649 + Current mass in system = 6.17869e-10 + Linear momentum = (2.81595e-11 -6.13881e-09 0) + |Linear momentum| = 6.13887e-09 + Linear kinetic energy = 3.20573e-08 + model1: + number of parcels added = 5651 + mass introduced = 6.23831e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.158, 507.409 + Mass transfer phase change = 5.96255e-12 + D10, D32, Dmax (mu) = 44.0324, 77.7179, 148.922 + Liquid penetration 95% mass (m) = 0.00327006 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00668031, Final residual = 1.96268e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0177007, Final residual = 4.46563e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.004129, Final residual = 3.66362e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00420139, Final residual = 2.01657e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00453217, Final residual = 2.25305e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00453219, Final residual = 2.25534e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0036347, Final residual = 2.71787e-07, No Iterations 1 +min/max(T) = 625.297, 827.79 +GAMG: Solving for p, Initial residual = 0.0305768, Final residual = 0.000344561, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.0548e-06, global = 1.02732e-06, cumulative = 0.000137599 +GAMG: Solving for p, Initial residual = 0.000345054, Final residual = 3.91136e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.01925e-06, global = 1.01921e-06, cumulative = 0.000138618 +smoothSolver: Solving for epsilon, Initial residual = 0.000856692, Final residual = 1.42532e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00572455, Final residual = 9.21356e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.067849 s +other Time = 1e-06 s +rho Equations = 0.000188 s +U Equations = 0.0014 s +Y Equations = 0.00225657 s +E Equations = 0.000527 s +p Equations = 0.00183 s +calculate parcels = 6.905 s +chemistry correctThermo = 0.001909 s +turbulence correct = 0.0009 s +combustion correct(in Y) = 0.0586094 s +percentage of chemistry = 86.3822 % +percentage of rho/U/Y/E = 6.44309 % +========Time details of each equation======= +rhoEqn Time = 0.000312 s +rhoEqn assamble = 0.000249 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001399 s +UEqn assamble = 0.000839 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00056 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001543 s +YEqn assamble = 0.000569 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 7.8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000401 s +EEqn assamble = 0.000303 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 20.39 s ClockTime = 21 s +Courant Number mean: 0.000216289 max: 0.0168354 +Time = 0.0003975 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 52 new parcels + +Cloud: sprayCloud + Current number of parcels = 5701 + Current mass in system = 6.22376e-10 + Linear momentum = (2.80079e-11 -6.18096e-09 0) + |Linear momentum| = 6.18102e-09 + Linear kinetic energy = 3.2271e-08 + model1: + number of parcels added = 5703 + mass introduced = 6.28428e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.146, 507.494 + Mass transfer phase change = 6.05169e-12 + D10, D32, Dmax (mu) = 44.097, 77.7053, 148.927 + Liquid penetration 95% mass (m) = 0.00328922 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00692418, Final residual = 2.06076e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0170971, Final residual = 4.33223e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00408745, Final residual = 3.6329e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00417109, Final residual = 1.99926e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00450186, Final residual = 2.24963e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00450188, Final residual = 2.25191e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00360546, Final residual = 2.68659e-07, No Iterations 1 +min/max(T) = 625.426, 828.129 +GAMG: Solving for p, Initial residual = 0.0312746, Final residual = 0.000388481, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.06476e-06, global = 1.03961e-06, cumulative = 0.000139657 +GAMG: Solving for p, Initial residual = 0.000387792, Final residual = 5.23445e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.02754e-06, global = 1.02749e-06, cumulative = 0.000140685 +smoothSolver: Solving for epsilon, Initial residual = 0.000859882, Final residual = 1.4292e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00568641, Final residual = 9.15076e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.06912 s +other Time = 0 s +rho Equations = 0.00016 s +U Equations = 0.001037 s +Y Equations = 0.00213342 s +E Equations = 0.000499 s +p Equations = 0.002363 s +calculate parcels = 6.98155 s +chemistry correctThermo = 0.002823 s +turbulence correct = 0.000995 s +combustion correct(in Y) = 0.0589166 s +percentage of chemistry = 85.2381 % +percentage of rho/U/Y/E = 5.54025 % +========Time details of each equation======= +rhoEqn Time = 0.00031 s +rhoEqn assamble = 0.00025 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001037 s +UEqn assamble = 0.00062 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000417 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001474 s +YEqn assamble = 0.000575 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.1e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000379 s +EEqn assamble = 0.000285 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 20.54 s ClockTime = 21 s +Courant Number mean: 0.000215159 max: 0.0168267 +Time = 0.0004 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 41 new parcels + +Cloud: sprayCloud + Current number of parcels = 5742 + Current mass in system = 6.25915e-10 + Linear momentum = (2.83152e-11 -6.21044e-09 0) + |Linear momentum| = 6.21051e-09 + Linear kinetic energy = 3.24008e-08 + model1: + number of parcels added = 5744 + mass introduced = 6.32056e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.158, 507.327 + Mass transfer phase change = 6.14151e-12 + D10, D32, Dmax (mu) = 44.1556, 77.7163, 148.932 + Liquid penetration 95% mass (m) = 0.00331034 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.007429, Final residual = 2.21143e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0163915, Final residual = 4.15926e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00409639, Final residual = 3.71696e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0041411, Final residual = 1.95838e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00447374, Final residual = 2.24946e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00447376, Final residual = 2.25173e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00356152, Final residual = 2.63476e-07, No Iterations 1 +min/max(T) = 625.552, 828.468 +GAMG: Solving for p, Initial residual = 0.0318725, Final residual = 0.000355507, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.06923e-06, global = 1.0441e-06, cumulative = 0.000141729 +GAMG: Solving for p, Initial residual = 0.000355471, Final residual = 5.06885e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.03529e-06, global = 1.03524e-06, cumulative = 0.000142764 +smoothSolver: Solving for epsilon, Initial residual = 0.00086402, Final residual = 1.43537e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00565064, Final residual = 9.096e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.093753 s +other Time = 1e-06 s +rho Equations = 0.000133 s +U Equations = 0.001688 s +Y Equations = 0.00266283 s +E Equations = 0.000677 s +p Equations = 0.00225 s +calculate parcels = 7.08218 s +chemistry correctThermo = 0.00287 s +turbulence correct = 0.000993 s +combustion correct(in Y) = 0.0823102 s +percentage of chemistry = 87.7947 % +percentage of rho/U/Y/E = 5.50471 % +========Time details of each equation======= +rhoEqn Time = 0.000278 s +rhoEqn assamble = 0.000222 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001686 s +UEqn assamble = 0.000838 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000848 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002062 s +YEqn assamble = 0.000768 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000258 s +YEqn correct boundary = 0 s +EEqn Time = 0.000505 s +EEqn assamble = 0.000377 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000128 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 20.84 s ClockTime = 21 s +Courant Number mean: 0.000213951 max: 0.01686 +Time = 0.0004025 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 5791 + Current mass in system = 6.30146e-10 + Linear momentum = (2.82034e-11 -6.2489e-09 0) + |Linear momentum| = 6.24897e-09 + Linear kinetic energy = 3.25892e-08 + model1: + number of parcels added = 5793 + mass introduced = 6.36378e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.14, 507.113 + Mass transfer phase change = 6.23223e-12 + D10, D32, Dmax (mu) = 43.4338, 77.6272, 148.938 + Liquid penetration 95% mass (m) = 0.00333275 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00723912, Final residual = 2.26946e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0158546, Final residual = 4.08377e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0040336, Final residual = 3.5988e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00411616, Final residual = 1.96004e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00444483, Final residual = 2.24826e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00444485, Final residual = 2.25053e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00353809, Final residual = 2.61021e-07, No Iterations 1 +min/max(T) = 625.675, 828.813 +GAMG: Solving for p, Initial residual = 0.0327873, Final residual = 0.000433156, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.08591e-06, global = 1.0565e-06, cumulative = 0.000143821 +GAMG: Solving for p, Initial residual = 0.000437513, Final residual = 7.97795e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.04572e-06, global = 1.04565e-06, cumulative = 0.000144866 +smoothSolver: Solving for epsilon, Initial residual = 0.000867474, Final residual = 1.44062e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00561477, Final residual = 9.04166e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095263 s +other Time = 0 s +rho Equations = 0.000158 s +U Equations = 0.001184 s +Y Equations = 0.00236044 s +E Equations = 0.000608 s +p Equations = 0.002202 s +calculate parcels = 7.18096 s +chemistry correctThermo = 0.002822 s +turbulence correct = 0.000988 s +combustion correct(in Y) = 0.0847516 s +percentage of chemistry = 88.9659 % +percentage of rho/U/Y/E = 4.52478 % +========Time details of each equation======= +rhoEqn Time = 0.000301 s +rhoEqn assamble = 0.000238 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001184 s +UEqn assamble = 0.000679 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000505 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001696 s +YEqn assamble = 0.000627 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000161 s +YEqn correct boundary = 0 s +EEqn Time = 0.000451 s +EEqn assamble = 0.000338 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 21.04 s ClockTime = 21 s +Courant Number mean: 0.000212766 max: 0.0168825 +Time = 0.000405 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 56 new parcels + +Cloud: sprayCloud + Current number of parcels = 5847 + Current mass in system = 6.34995e-10 + Linear momentum = (2.85234e-11 -6.29533e-09 0) + |Linear momentum| = 6.29539e-09 + Linear kinetic energy = 3.28309e-08 + model1: + number of parcels added = 5849 + mass introduced = 6.41318e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.141, 506.859 + Mass transfer phase change = 6.32364e-12 + D10, D32, Dmax (mu) = 43.5201, 77.671, 148.991 + Liquid penetration 95% mass (m) = 0.00335409 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00737977, Final residual = 2.1638e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0154922, Final residual = 4.00699e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0039938, Final residual = 3.53599e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00408803, Final residual = 1.94913e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00441853, Final residual = 2.24524e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00441855, Final residual = 2.2475e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00350011, Final residual = 2.55792e-07, No Iterations 1 +min/max(T) = 625.779, 829.154 +GAMG: Solving for p, Initial residual = 0.0334199, Final residual = 0.00038289, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.08757e-06, global = 1.06074e-06, cumulative = 0.000145927 +GAMG: Solving for p, Initial residual = 0.000383993, Final residual = 5.98125e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.05364e-06, global = 1.05359e-06, cumulative = 0.000146981 +smoothSolver: Solving for epsilon, Initial residual = 0.00087163, Final residual = 1.44746e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00558082, Final residual = 8.99357e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.08874 s +other Time = 0 s +rho Equations = 0.000141 s +U Equations = 0.001011 s +Y Equations = 0.00218879 s +E Equations = 0.000505 s +p Equations = 0.001871 s +calculate parcels = 7.28655 s +chemistry correctThermo = 0.002023 s +turbulence correct = 0.000844 s +combustion correct(in Y) = 0.0799872 s +percentage of chemistry = 90.1366 % +percentage of rho/U/Y/E = 4.33377 % +========Time details of each equation======= +rhoEqn Time = 0.000281 s +rhoEqn assamble = 0.000215 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001009 s +UEqn assamble = 0.000589 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00042 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001615 s +YEqn assamble = 0.000569 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000154 s +YEqn correct boundary = 0 s +EEqn Time = 0.000381 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 21.23 s ClockTime = 22 s +Courant Number mean: 0.000211496 max: 0.0169073 +Time = 0.0004075 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 5893 + Current mass in system = 6.38973e-10 + Linear momentum = (2.86479e-11 -6.3304e-09 0) + |Linear momentum| = 6.33046e-09 + Linear kinetic energy = 3.29971e-08 + model1: + number of parcels added = 5895 + mass introduced = 6.45389e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.138, 506.568 + Mass transfer phase change = 6.41576e-12 + D10, D32, Dmax (mu) = 43.5441, 77.6762, 148.948 + Liquid penetration 95% mass (m) = 0.00337364 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00720099, Final residual = 2.12523e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0158009, Final residual = 4.10257e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00393622, Final residual = 3.50266e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00406079, Final residual = 1.97146e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00439108, Final residual = 2.24142e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0043911, Final residual = 2.24364e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00345384, Final residual = 2.54912e-07, No Iterations 1 +min/max(T) = 625.904, 829.5 +GAMG: Solving for p, Initial residual = 0.0337791, Final residual = 0.000377277, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.09596e-06, global = 1.06877e-06, cumulative = 0.00014805 +GAMG: Solving for p, Initial residual = 0.000377853, Final residual = 5.21487e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.06179e-06, global = 1.06174e-06, cumulative = 0.000149111 +smoothSolver: Solving for epsilon, Initial residual = 0.000875981, Final residual = 1.45509e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00554803, Final residual = 8.94887e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094695 s +other Time = 0 s +rho Equations = 0.000156 s +U Equations = 0.001181 s +Y Equations = 0.00244189 s +E Equations = 0.000634 s +p Equations = 0.002282 s +calculate parcels = 7.38187 s +chemistry correctThermo = 0.00276 s +turbulence correct = 0.000998 s +combustion correct(in Y) = 0.0840521 s +percentage of chemistry = 88.7609 % +percentage of rho/U/Y/E = 4.6601 % +========Time details of each equation======= +rhoEqn Time = 0.000299 s +rhoEqn assamble = 0.000236 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001181 s +UEqn assamble = 0.000674 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000507 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001756 s +YEqn assamble = 0.000665 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000155 s +YEqn correct boundary = 0 s +EEqn Time = 0.000471 s +EEqn assamble = 0.000344 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000127 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 21.42 s ClockTime = 22 s +Courant Number mean: 0.000210182 max: 0.0169395 +Time = 0.00041 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 56 new parcels + +Cloud: sprayCloud + Current number of parcels = 5949 + Current mass in system = 6.43829e-10 + Linear momentum = (2.73644e-11 -6.37677e-09 0) + |Linear momentum| = 6.37683e-09 + Linear kinetic energy = 3.32388e-08 + model1: + number of parcels added = 5951 + mass introduced = 6.50337e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.138, 506.243 + Mass transfer phase change = 6.50859e-12 + D10, D32, Dmax (mu) = 43.627, 77.7154, 149.203 + Liquid penetration 95% mass (m) = 0.00339437 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0068593, Final residual = 1.97068e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0161067, Final residual = 4.21582e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00390876, Final residual = 3.5051e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0040356, Final residual = 1.96925e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00436603, Final residual = 2.23821e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00436605, Final residual = 2.24043e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00342456, Final residual = 2.51374e-07, No Iterations 1 +min/max(T) = 626.007, 829.848 +GAMG: Solving for p, Initial residual = 0.0337712, Final residual = 0.000348324, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.10077e-06, global = 1.0751e-06, cumulative = 0.000150186 +GAMG: Solving for p, Initial residual = 0.000349781, Final residual = 4.112e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.07002e-06, global = 1.06998e-06, cumulative = 0.000151256 +smoothSolver: Solving for epsilon, Initial residual = 0.000880354, Final residual = 1.46279e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00551593, Final residual = 8.90614e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.082369 s +other Time = 1e-06 s +rho Equations = 0.000163 s +U Equations = 0.0012 s +Y Equations = 0.00200829 s +E Equations = 0.000489 s +p Equations = 0.001783 s +calculate parcels = 7.48118 s +chemistry correctThermo = 0.00197 s +turbulence correct = 0.000838 s +combustion correct(in Y) = 0.0737327 s +percentage of chemistry = 89.5151 % +percentage of rho/U/Y/E = 4.68658 % +========Time details of each equation======= +rhoEqn Time = 0.000292 s +rhoEqn assamble = 0.000232 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001198 s +UEqn assamble = 0.000706 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000492 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001322 s +YEqn assamble = 0.00051 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 7.5e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000371 s +EEqn assamble = 0.000279 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 21.61 s ClockTime = 22 s +Courant Number mean: 0.000208835 max: 0.0169677 +Time = 0.0004125 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 5996 + Current mass in system = 6.4799e-10 + Linear momentum = (2.76288e-11 -6.41405e-09 0) + |Linear momentum| = 6.41411e-09 + Linear kinetic energy = 3.34203e-08 + model1: + number of parcels added = 5999 + mass introduced = 6.54593e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.142, 505.886 + Mass transfer phase change = 6.60296e-12 + D10, D32, Dmax (mu) = 44.8209, 77.773, 148.959 + Liquid penetration 95% mass (m) = 0.00341472 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00671013, Final residual = 1.89628e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0162972, Final residual = 4.29054e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00391501, Final residual = 3.54565e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00402493, Final residual = 1.95989e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00434009, Final residual = 2.23247e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00434011, Final residual = 2.23468e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00337936, Final residual = 2.43825e-07, No Iterations 1 +min/max(T) = 626.091, 830.195 +GAMG: Solving for p, Initial residual = 0.0345262, Final residual = 0.000440126, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.12167e-06, global = 1.09498e-06, cumulative = 0.000152351 +GAMG: Solving for p, Initial residual = 0.00044486, Final residual = 4.28795e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.08768e-06, global = 1.08765e-06, cumulative = 0.000153439 +smoothSolver: Solving for epsilon, Initial residual = 0.00088537, Final residual = 1.47265e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00548453, Final residual = 8.86814e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.090543 s +other Time = 0 s +rho Equations = 0.00014 s +U Equations = 0.000993 s +Y Equations = 0.00255701 s +E Equations = 0.000682 s +p Equations = 0.002701 s +calculate parcels = 7.56885 s +chemistry correctThermo = 0.002784 s +turbulence correct = 0.001032 s +combustion correct(in Y) = 0.079461 s +percentage of chemistry = 87.7605 % +percentage of rho/U/Y/E = 4.82866 % +========Time details of each equation======= +rhoEqn Time = 0.000313 s +rhoEqn assamble = 0.000248 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000992 s +UEqn assamble = 0.000575 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000417 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002008 s +YEqn assamble = 0.000714 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000281 s +YEqn correct boundary = 0 s +EEqn Time = 0.000504 s +EEqn assamble = 0.000379 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000125 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 21.78 s ClockTime = 22 s +Courant Number mean: 0.000207411 max: 0.0170297 +Time = 0.000415 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 54 new parcels + +Cloud: sprayCloud + Current number of parcels = 6050 + Current mass in system = 6.52681e-10 + Linear momentum = (2.86649e-11 -6.45835e-09 0) + |Linear momentum| = 6.45841e-09 + Linear kinetic energy = 3.36478e-08 + model1: + number of parcels added = 6053 + mass introduced = 6.59378e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.147, 505.662 + Mass transfer phase change = 6.69689e-12 + D10, D32, Dmax (mu) = 44.9055, 77.8059, 148.964 + Liquid penetration 95% mass (m) = 0.00343481 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00627259, Final residual = 9.67134e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0165689, Final residual = 4.40921e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00385655, Final residual = 3.47418e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0039791, Final residual = 1.91706e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00431534, Final residual = 2.22746e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00431536, Final residual = 2.22965e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00334241, Final residual = 2.38278e-07, No Iterations 1 +min/max(T) = 626.149, 830.547 +GAMG: Solving for p, Initial residual = 0.0344237, Final residual = 0.000423402, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.11849e-06, global = 1.086e-06, cumulative = 0.000154525 +GAMG: Solving for p, Initial residual = 0.000426377, Final residual = 4.03266e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.08267e-06, global = 1.08263e-06, cumulative = 0.000155608 +smoothSolver: Solving for epsilon, Initial residual = 0.000890408, Final residual = 1.48305e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00545465, Final residual = 8.8364e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.08314 s +other Time = 0 s +rho Equations = 0.000152 s +U Equations = 0.001111 s +Y Equations = 0.00241108 s +E Equations = 0.000761 s +p Equations = 0.002535 s +calculate parcels = 7.66223 s +chemistry correctThermo = 0.002929 s +turbulence correct = 0.00101 s +combustion correct(in Y) = 0.0720339 s +percentage of chemistry = 86.6417 % +percentage of rho/U/Y/E = 5.33447 % +========Time details of each equation======= +rhoEqn Time = 0.000324 s +rhoEqn assamble = 0.000259 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00111 s +UEqn assamble = 0.00068 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00043 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001744 s +YEqn assamble = 0.000659 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000185 s +YEqn correct boundary = 0 s +EEqn Time = 0.000588 s +EEqn assamble = 0.00044 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000148 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 21.96 s ClockTime = 22 s +Courant Number mean: 0.000205971 max: 0.0170619 +Time = 0.0004175 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 54 new parcels + +Cloud: sprayCloud + Current number of parcels = 6104 + Current mass in system = 6.57382e-10 + Linear momentum = (3.01971e-11 -6.50268e-09 0) + |Linear momentum| = 6.50275e-09 + Linear kinetic energy = 3.3876e-08 + model1: + number of parcels added = 6107 + mass introduced = 6.64173e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.148, 505.945 + Mass transfer phase change = 6.79147e-12 + D10, D32, Dmax (mu) = 44.9577, 77.829, 148.97 + Liquid penetration 95% mass (m) = 0.00345491 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00604456, Final residual = 9.24976e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0166598, Final residual = 4.45051e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00383703, Final residual = 3.45266e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00395495, Final residual = 1.88929e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00429177, Final residual = 2.22139e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00429179, Final residual = 2.22357e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00330421, Final residual = 2.32027e-07, No Iterations 1 +min/max(T) = 626.198, 830.898 +GAMG: Solving for p, Initial residual = 0.0338133, Final residual = 0.000373417, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.11932e-06, global = 1.09338e-06, cumulative = 0.000156701 +GAMG: Solving for p, Initial residual = 0.000377739, Final residual = 2.95012e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.09022e-06, global = 1.0902e-06, cumulative = 0.000157791 +smoothSolver: Solving for epsilon, Initial residual = 0.000895374, Final residual = 1.49376e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00542478, Final residual = 8.80373e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.080444 s +other Time = 1e-06 s +rho Equations = 0.00018 s +U Equations = 0.001215 s +Y Equations = 0.00234645 s +E Equations = 0.000505 s +p Equations = 0.001859 s +calculate parcels = 7.76715 s +chemistry correctThermo = 0.002186 s +turbulence correct = 0.000841 s +combustion correct(in Y) = 0.0711026 s +percentage of chemistry = 88.3876 % +percentage of rho/U/Y/E = 5.27877 % +========Time details of each equation======= +rhoEqn Time = 0.000304 s +rhoEqn assamble = 0.000239 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001214 s +UEqn assamble = 0.000751 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000463 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001595 s +YEqn assamble = 0.000722 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 5.2e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000385 s +EEqn assamble = 0.000287 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 22.15 s ClockTime = 23 s +Courant Number mean: 0.000204499 max: 0.0171083 +Time = 0.00042 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 57 new parcels + +Cloud: sprayCloud + Current number of parcels = 6161 + Current mass in system = 6.62357e-10 + Linear momentum = (2.85393e-11 -6.55056e-09 0) + |Linear momentum| = 6.55063e-09 + Linear kinetic energy = 3.41273e-08 + model1: + number of parcels added = 6164 + mass introduced = 6.69243e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.141, 506.196 + Mass transfer phase change = 6.88673e-12 + D10, D32, Dmax (mu) = 45.0421, 77.8945, 148.975 + Liquid penetration 95% mass (m) = 0.00347497 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00588203, Final residual = 8.99753e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0167754, Final residual = 4.48251e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00379825, Final residual = 3.42217e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00393193, Final residual = 1.87958e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00426834, Final residual = 2.21671e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00426836, Final residual = 2.21886e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00326857, Final residual = 2.30237e-07, No Iterations 1 +min/max(T) = 626.273, 831.25 +GAMG: Solving for p, Initial residual = 0.0332585, Final residual = 0.000380137, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.12437e-06, global = 1.10422e-06, cumulative = 0.000158895 +GAMG: Solving for p, Initial residual = 0.000383478, Final residual = 4.87109e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.098e-06, global = 1.09797e-06, cumulative = 0.000159993 +smoothSolver: Solving for epsilon, Initial residual = 0.000900113, Final residual = 1.50435e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00539522, Final residual = 8.771e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092099 s +other Time = 1e-06 s +rho Equations = 0.000229 s +U Equations = 0.001548 s +Y Equations = 0.00228663 s +E Equations = 0.000501 s +p Equations = 0.001828 s +calculate parcels = 7.87723 s +chemistry correctThermo = 0.002027 s +turbulence correct = 0.000816 s +combustion correct(in Y) = 0.0826254 s +percentage of chemistry = 89.7136 % +percentage of rho/U/Y/E = 4.95622 % +========Time details of each equation======= +rhoEqn Time = 0.000343 s +rhoEqn assamble = 0.000265 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001546 s +UEqn assamble = 0.000896 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00065 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001073 s +YEqn assamble = 0.000524 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -0.000199 s +YEqn correct boundary = 0 s +EEqn Time = 0.000379 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 22.35 s ClockTime = 23 s +Courant Number mean: 0.000203039 max: 0.0171503 +Time = 0.0004225 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 53 new parcels + +Cloud: sprayCloud + Current number of parcels = 6214 + Current mass in system = 6.66988e-10 + Linear momentum = (2.70841e-11 -6.5939e-09 0) + |Linear momentum| = 6.59396e-09 + Linear kinetic energy = 3.43478e-08 + model1: + number of parcels added = 6217 + mass introduced = 6.73971e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.154, 506.416 + Mass transfer phase change = 6.98279e-12 + D10, D32, Dmax (mu) = 45.1002, 77.9003, 148.981 + Liquid penetration 95% mass (m) = 0.00349484 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00570614, Final residual = 8.54205e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0169099, Final residual = 4.51144e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0037563, Final residual = 3.38948e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00391134, Final residual = 1.86581e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0042447, Final residual = 2.21152e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00424472, Final residual = 2.21366e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00323389, Final residual = 2.28273e-07, No Iterations 1 +min/max(T) = 626.375, 831.602 +GAMG: Solving for p, Initial residual = 0.0331552, Final residual = 0.00040838, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.1355e-06, global = 1.1114e-06, cumulative = 0.000161105 +GAMG: Solving for p, Initial residual = 0.000409637, Final residual = 5.90429e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.10713e-06, global = 1.1071e-06, cumulative = 0.000162212 +smoothSolver: Solving for epsilon, Initial residual = 0.000904729, Final residual = 1.51495e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00536575, Final residual = 8.73866e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095382 s +other Time = 0 s +rho Equations = 0.000159 s +U Equations = 0.001097 s +Y Equations = 0.00235982 s +E Equations = 0.000616 s +p Equations = 0.002246 s +calculate parcels = 7.98249 s +chemistry correctThermo = 0.002793 s +turbulence correct = 0.001076 s +combustion correct(in Y) = 0.0848362 s +percentage of chemistry = 88.9436 % +percentage of rho/U/Y/E = 4.4367 % +========Time details of each equation======= +rhoEqn Time = 0.000307 s +rhoEqn assamble = 0.000243 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001095 s +UEqn assamble = 0.000669 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000426 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001705 s +YEqn assamble = 0.000636 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000184 s +YEqn correct boundary = 0 s +EEqn Time = 0.000457 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000122 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 22.55 s ClockTime = 23 s +Courant Number mean: 0.000201639 max: 0.0171879 +Time = 0.000425 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 6263 + Current mass in system = 6.71266e-10 + Linear momentum = (2.55723e-11 -6.63252e-09 0) + |Linear momentum| = 6.63257e-09 + Linear kinetic energy = 3.45367e-08 + model1: + number of parcels added = 6266 + mass introduced = 6.78345e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.159, 506.595 + Mass transfer phase change = 7.07962e-12 + D10, D32, Dmax (mu) = 45.1154, 77.9075, 148.986 + Liquid penetration 95% mass (m) = 0.00351431 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00561832, Final residual = 8.27959e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0170418, Final residual = 4.52824e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00371973, Final residual = 3.32356e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00389136, Final residual = 1.85062e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00422173, Final residual = 2.20449e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00422175, Final residual = 2.20661e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00320929, Final residual = 2.23347e-07, No Iterations 1 +min/max(T) = 626.462, 831.955 +GAMG: Solving for p, Initial residual = 0.0332369, Final residual = 0.000377258, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.14148e-06, global = 1.12021e-06, cumulative = 0.000163332 +GAMG: Solving for p, Initial residual = 0.000381965, Final residual = 4.22007e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.1161e-06, global = 1.11607e-06, cumulative = 0.000164448 +smoothSolver: Solving for epsilon, Initial residual = 0.000909498, Final residual = 1.52603e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00533665, Final residual = 8.70758e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.067407 s +other Time = 0 s +rho Equations = 0.000157 s +U Equations = 0.000999 s +Y Equations = 0.00209986 s +E Equations = 0.000505 s +p Equations = 0.001884 s +calculate parcels = 8.08339 s +chemistry correctThermo = 0.001944 s +turbulence correct = 0.000869 s +combustion correct(in Y) = 0.0587621 s +percentage of chemistry = 87.1751 % +percentage of rho/U/Y/E = 5.57934 % +========Time details of each equation======= +rhoEqn Time = 0.000279 s +rhoEqn assamble = 0.000225 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000999 s +UEqn assamble = 0.00064 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000359 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001541 s +YEqn assamble = 0.00057 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000135 s +YEqn correct boundary = 0 s +EEqn Time = 0.000383 s +EEqn assamble = 0.000288 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 22.72 s ClockTime = 23 s +Courant Number mean: 0.000200261 max: 0.0172365 +Time = 0.0004275 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 6309 + Current mass in system = 6.75272e-10 + Linear momentum = (2.68549e-11 -6.66747e-09 0) + |Linear momentum| = 6.66752e-09 + Linear kinetic energy = 3.47011e-08 + model1: + number of parcels added = 6312 + mass introduced = 6.82449e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.141, 506.688 + Mass transfer phase change = 7.17718e-12 + D10, D32, Dmax (mu) = 45.1491, 77.8823, 148.991 + Liquid penetration 95% mass (m) = 0.00353293 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00567909, Final residual = 8.20014e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0170926, Final residual = 4.53502e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00367813, Final residual = 3.25268e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00387105, Final residual = 1.8265e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00419917, Final residual = 2.19565e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00419918, Final residual = 2.19776e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0031862, Final residual = 2.20152e-07, No Iterations 1 +min/max(T) = 626.564, 832.31 +GAMG: Solving for p, Initial residual = 0.0336876, Final residual = 0.000391064, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.15078e-06, global = 1.12947e-06, cumulative = 0.000165578 +GAMG: Solving for p, Initial residual = 0.000395315, Final residual = 3.87708e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.12451e-06, global = 1.12449e-06, cumulative = 0.000166702 +smoothSolver: Solving for epsilon, Initial residual = 0.000914304, Final residual = 1.53705e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00530815, Final residual = 8.6768e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.066852 s +other Time = 0 s +rho Equations = 0.000155 s +U Equations = 0.00099 s +Y Equations = 0.00213042 s +E Equations = 0.000799 s +p Equations = 0.001915 s +calculate parcels = 8.16871 s +chemistry correctThermo = 0.001885 s +turbulence correct = 0.000814 s +combustion correct(in Y) = 0.0579886 s +percentage of chemistry = 86.7417 % +percentage of rho/U/Y/E = 6.09469 % +========Time details of each equation======= +rhoEqn Time = 0.000294 s +rhoEqn assamble = 0.000224 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000989 s +UEqn assamble = 0.000629 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00036 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001406 s +YEqn assamble = 0.000546 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 4.8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000675 s +EEqn assamble = 0.000556 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000119 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 22.87 s ClockTime = 23 s +Courant Number mean: 0.000198936 max: 0.0172875 +Time = 0.00043 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 36 new parcels + +Cloud: sprayCloud + Current number of parcels = 6343 + Current mass in system = 6.78377e-10 + Linear momentum = (2.68993e-11 -6.69059e-09 0) + |Linear momentum| = 6.69064e-09 + Linear kinetic energy = 3.47874e-08 + model1: + number of parcels added = 6348 + mass introduced = 6.85654e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.141, 506.693 + Mass transfer phase change = 7.27721e-12 + D10, D32, Dmax (mu) = 50.171, 77.9007, 148.997 + Liquid penetration 95% mass (m) = 0.00355224 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00547811, Final residual = 7.48892e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0168911, Final residual = 4.51566e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00367147, Final residual = 3.0783e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00387884, Final residual = 1.84079e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00417586, Final residual = 2.18405e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00417587, Final residual = 2.18614e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00317411, Final residual = 2.13661e-07, No Iterations 1 +min/max(T) = 626.641, 832.666 +GAMG: Solving for p, Initial residual = 0.035691, Final residual = 0.000591986, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.18874e-06, global = 1.16378e-06, cumulative = 0.000167866 +GAMG: Solving for p, Initial residual = 0.000605547, Final residual = 6.53123e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.15299e-06, global = 1.15294e-06, cumulative = 0.000169019 +smoothSolver: Solving for epsilon, Initial residual = 0.000919622, Final residual = 1.54866e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0052794, Final residual = 8.64361e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.082854 s +other Time = 0 s +rho Equations = 0.000132 s +U Equations = 0.000943 s +Y Equations = 0.00198224 s +E Equations = 0.000491 s +p Equations = 0.003657 s +calculate parcels = 8.26373 s +chemistry correctThermo = 0.004301 s +turbulence correct = 0.001651 s +combustion correct(in Y) = 0.0694988 s +percentage of chemistry = 83.881 % +percentage of rho/U/Y/E = 4.28252 % +========Time details of each equation======= +rhoEqn Time = 0.000414 s +rhoEqn assamble = 0.000314 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.0001 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000942 s +UEqn assamble = 0.000582 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00036 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001343 s +YEqn assamble = 0.000502 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.5e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000371 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 23.05 s ClockTime = 23 s +Courant Number mean: 0.0001976 max: 0.0173606 +Time = 0.0004325 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 6389 + Current mass in system = 6.82347e-10 + Linear momentum = (2.80051e-11 -6.72501e-09 0) + |Linear momentum| = 6.72507e-09 + Linear kinetic energy = 3.4948e-08 + model1: + number of parcels added = 6394 + mass introduced = 6.89723e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.137, 506.621 + Mass transfer phase change = 7.3757e-12 + D10, D32, Dmax (mu) = 49.9875, 77.8935, 149.002 + Liquid penetration 95% mass (m) = 0.00357189 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00526627, Final residual = 7.293e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0166883, Final residual = 4.53551e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00364704, Final residual = 3.19472e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00382131, Final residual = 1.75897e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00415477, Final residual = 2.1767e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00415479, Final residual = 2.17878e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00313693, Final residual = 2.08453e-07, No Iterations 1 +min/max(T) = 626.741, 833.027 +GAMG: Solving for p, Initial residual = 0.0372326, Final residual = 0.000561848, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.1692e-06, global = 1.14087e-06, cumulative = 0.00017016 +GAMG: Solving for p, Initial residual = 0.000571688, Final residual = 5.86298e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.13525e-06, global = 1.13521e-06, cumulative = 0.000171295 +smoothSolver: Solving for epsilon, Initial residual = 0.000925207, Final residual = 1.56189e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00525367, Final residual = 8.62217e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095362 s +other Time = 0 s +rho Equations = 0.000164 s +U Equations = 0.001162 s +Y Equations = 0.00236031 s +E Equations = 0.000612 s +p Equations = 0.002185 s +calculate parcels = 8.37121 s +chemistry correctThermo = 0.002787 s +turbulence correct = 0.000973 s +combustion correct(in Y) = 0.0849287 s +percentage of chemistry = 89.0593 % +percentage of rho/U/Y/E = 4.50736 % +========Time details of each equation======= +rhoEqn Time = 0.000318 s +rhoEqn assamble = 0.000251 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001162 s +UEqn assamble = 0.00069 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000472 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001717 s +YEqn assamble = 0.000649 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000168 s +YEqn correct boundary = 0 s +EEqn Time = 0.000455 s +EEqn assamble = 0.000341 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 23.25 s ClockTime = 24 s +Courant Number mean: 0.000196414 max: 0.0173895 +Time = 0.000435 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 6439 + Current mass in system = 6.86662e-10 + Linear momentum = (2.68765e-11 -6.7639e-09 0) + |Linear momentum| = 6.76395e-09 + Linear kinetic energy = 3.51382e-08 + model1: + number of parcels added = 6444 + mass introduced = 6.94137e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.14, 506.474 + Mass transfer phase change = 7.47502e-12 + D10, D32, Dmax (mu) = 50.0505, 77.9324, 149.008 + Liquid penetration 95% mass (m) = 0.00359242 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00479847, Final residual = 6.41041e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0160642, Final residual = 4.45378e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00361206, Final residual = 3.1233e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00380421, Final residual = 1.74832e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00413315, Final residual = 2.16792e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00413317, Final residual = 2.16995e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00311881, Final residual = 2.0401e-07, No Iterations 1 +min/max(T) = 626.864, 833.385 +GAMG: Solving for p, Initial residual = 0.0368987, Final residual = 0.000357005, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.16544e-06, global = 1.14911e-06, cumulative = 0.000172444 +GAMG: Solving for p, Initial residual = 0.000358722, Final residual = 5.45733e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.14476e-06, global = 1.14473e-06, cumulative = 0.000173589 +smoothSolver: Solving for epsilon, Initial residual = 0.000930439, Final residual = 1.57444e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00522702, Final residual = 8.59628e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092597 s +other Time = 1e-06 s +rho Equations = 0.000166 s +U Equations = 0.001141 s +Y Equations = 0.00239384 s +E Equations = 0.000608 s +p Equations = 0.002279 s +calculate parcels = 8.48982 s +chemistry correctThermo = 0.00287 s +turbulence correct = 0.000977 s +combustion correct(in Y) = 0.0819582 s +percentage of chemistry = 88.5106 % +percentage of rho/U/Y/E = 4.65333 % +========Time details of each equation======= +rhoEqn Time = 0.000318 s +rhoEqn assamble = 0.000252 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00114 s +UEqn assamble = 0.000697 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000443 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001683 s +YEqn assamble = 0.000664 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000144 s +YEqn correct boundary = 0 s +EEqn Time = 0.000453 s +EEqn assamble = 0.000339 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 23.46 s ClockTime = 24 s +Courant Number mean: 0.000195321 max: 0.0174299 +Time = 0.0004375 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 42 new parcels + +Cloud: sprayCloud + Current number of parcels = 6481 + Current mass in system = 6.90268e-10 + Linear momentum = (2.68976e-11 -6.79349e-09 0) + |Linear momentum| = 6.79355e-09 + Linear kinetic energy = 3.52669e-08 + model1: + number of parcels added = 6486 + mass introduced = 6.97843e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.146, 506.255 + Mass transfer phase change = 7.57515e-12 + D10, D32, Dmax (mu) = 50.1162, 77.9501, 149.013 + Liquid penetration 95% mass (m) = 0.00361127 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00463355, Final residual = 6.12913e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0153755, Final residual = 4.29843e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00358907, Final residual = 3.04514e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00378691, Final residual = 1.72676e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00411141, Final residual = 2.15806e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00411143, Final residual = 2.16008e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00310301, Final residual = 1.9776e-07, No Iterations 1 +min/max(T) = 626.997, 833.745 +GAMG: Solving for p, Initial residual = 0.0392999, Final residual = 0.000464168, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.17585e-06, global = 1.15887e-06, cumulative = 0.000174748 +GAMG: Solving for p, Initial residual = 0.00047214, Final residual = 6.56753e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.15418e-06, global = 1.15414e-06, cumulative = 0.000175902 +smoothSolver: Solving for epsilon, Initial residual = 0.000935884, Final residual = 1.58741e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00520078, Final residual = 8.57034e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.087193 s +other Time = 1e-06 s +rho Equations = 0.000164 s +U Equations = 0.001099 s +Y Equations = 0.00214873 s +E Equations = 0.000495 s +p Equations = 0.001795 s +calculate parcels = 8.61078 s +chemistry correctThermo = 0.001986 s +turbulence correct = 0.000841 s +combustion correct(in Y) = 0.0784783 s +percentage of chemistry = 90.0052 % +percentage of rho/U/Y/E = 4.48055 % +========Time details of each equation======= +rhoEqn Time = 0.000286 s +rhoEqn assamble = 0.000224 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001099 s +UEqn assamble = 0.000672 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000427 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001425 s +YEqn assamble = 0.000555 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.2e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000373 s +EEqn assamble = 0.000279 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 23.67 s ClockTime = 24 s +Courant Number mean: 0.000194272 max: 0.0174784 +Time = 0.00044 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 6527 + Current mass in system = 6.94211e-10 + Linear momentum = (2.78079e-11 -6.8274e-09 0) + |Linear momentum| = 6.82746e-09 + Linear kinetic energy = 3.54244e-08 + model1: + number of parcels added = 6532 + mass introduced = 7.01887e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.153, 506.178 + Mass transfer phase change = 7.67617e-12 + D10, D32, Dmax (mu) = 50.1731, 77.9367, 149.018 + Liquid penetration 95% mass (m) = 0.00363126 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00459134, Final residual = 6.0578e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0146412, Final residual = 4.11597e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00355638, Final residual = 2.9746e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00377172, Final residual = 1.7117e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00409095, Final residual = 2.1482e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00409097, Final residual = 2.15018e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0030956, Final residual = 1.9443e-07, No Iterations 1 +min/max(T) = 627.151, 834.108 +GAMG: Solving for p, Initial residual = 0.0406926, Final residual = 0.000569018, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.19348e-06, global = 1.17127e-06, cumulative = 0.000177073 +GAMG: Solving for p, Initial residual = 0.000565678, Final residual = 1.82505e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.16439e-06, global = 1.16438e-06, cumulative = 0.000178237 +smoothSolver: Solving for epsilon, Initial residual = 0.000940752, Final residual = 1.59896e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00517417, Final residual = 8.54105e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094976 s +other Time = 0 s +rho Equations = 0.000167 s +U Equations = 0.001093 s +Y Equations = 0.00230117 s +E Equations = 0.000606 s +p Equations = 0.002475 s +calculate parcels = 8.71627 s +chemistry correctThermo = 0.002776 s +turbulence correct = 0.000994 s +combustion correct(in Y) = 0.0843458 s +percentage of chemistry = 88.8075 % +percentage of rho/U/Y/E = 4.3876 % +========Time details of each equation======= +rhoEqn Time = 0.000333 s +rhoEqn assamble = 0.000265 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001092 s +UEqn assamble = 0.000706 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000386 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001723 s +YEqn assamble = 0.000637 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000206 s +YEqn correct boundary = 0 s +EEqn Time = 0.000448 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 23.87 s ClockTime = 24 s +Courant Number mean: 0.000193332 max: 0.0175054 +Time = 0.0004425 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 6571 + Current mass in system = 6.97969e-10 + Linear momentum = (2.72993e-11 -6.85891e-09 0) + |Linear momentum| = 6.85896e-09 + Linear kinetic energy = 3.55653e-08 + model1: + number of parcels added = 6576 + mass introduced = 7.05747e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.158, 506.415 + Mass transfer phase change = 7.77808e-12 + D10, D32, Dmax (mu) = 50.0877, 77.8926, 149.024 + Liquid penetration 95% mass (m) = 0.00364975 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00454683, Final residual = 5.71909e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0137888, Final residual = 3.90089e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00352179, Final residual = 2.91075e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00375516, Final residual = 1.70757e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00406857, Final residual = 2.13692e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00406858, Final residual = 2.13888e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0030894, Final residual = 1.90937e-07, No Iterations 1 +min/max(T) = 627.311, 834.469 +GAMG: Solving for p, Initial residual = 0.0418566, Final residual = 0.000564312, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.20223e-06, global = 1.18149e-06, cumulative = 0.000179419 +GAMG: Solving for p, Initial residual = 0.000550242, Final residual = 9.11692e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.17463e-06, global = 1.17459e-06, cumulative = 0.000180594 +smoothSolver: Solving for epsilon, Initial residual = 0.000945374, Final residual = 1.61015e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00514744, Final residual = 8.50982e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.085158 s +other Time = 0 s +rho Equations = 0.00016 s +U Equations = 0.001143 s +Y Equations = 0.00211923 s +E Equations = 0.000506 s +p Equations = 0.001911 s +calculate parcels = 8.82701 s +chemistry correctThermo = 0.002015 s +turbulence correct = 0.000845 s +combustion correct(in Y) = 0.0762708 s +percentage of chemistry = 89.5638 % +percentage of rho/U/Y/E = 4.61287 % +========Time details of each equation======= +rhoEqn Time = 0.000295 s +rhoEqn assamble = 0.000236 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001141 s +UEqn assamble = 0.000705 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000436 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001449 s +YEqn assamble = 0.000543 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.1e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.00038 s +EEqn assamble = 0.000282 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 24.07 s ClockTime = 24 s +Courant Number mean: 0.000192609 max: 0.0175513 +Time = 0.000445 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 6621 + Current mass in system = 7.0224e-10 + Linear momentum = (2.65209e-11 -6.89701e-09 0) + |Linear momentum| = 6.89706e-09 + Linear kinetic energy = 3.57501e-08 + model1: + number of parcels added = 6626 + mass introduced = 7.10121e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.149, 506.649 + Mass transfer phase change = 7.88084e-12 + D10, D32, Dmax (mu) = 50.082, 77.881, 149.029 + Liquid penetration 95% mass (m) = 0.00366874 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00470875, Final residual = 5.89146e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0130352, Final residual = 3.67096e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00351001, Final residual = 2.86755e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00373814, Final residual = 1.70377e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00404692, Final residual = 2.12403e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00404694, Final residual = 2.12597e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.003079, Final residual = 1.87584e-07, No Iterations 1 +min/max(T) = 627.471, 834.831 +GAMG: Solving for p, Initial residual = 0.043827, Final residual = 0.00057592, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.21239e-06, global = 1.19154e-06, cumulative = 0.000181785 +GAMG: Solving for p, Initial residual = 0.000563484, Final residual = 9.3632e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.18446e-06, global = 1.18441e-06, cumulative = 0.000182969 +smoothSolver: Solving for epsilon, Initial residual = 0.000950118, Final residual = 1.6211e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00512085, Final residual = 8.47715e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.087791 s +other Time = 0 s +rho Equations = 0.000146 s +U Equations = 0.000951 s +Y Equations = 0.00237641 s +E Equations = 0.000611 s +p Equations = 0.002159 s +calculate parcels = 8.94449 s +chemistry correctThermo = 0.002774 s +turbulence correct = 0.001009 s +combustion correct(in Y) = 0.0775806 s +percentage of chemistry = 88.3696 % +percentage of rho/U/Y/E = 4.65243 % +========Time details of each equation======= +rhoEqn Time = 0.000285 s +rhoEqn assamble = 0.000227 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00095 s +UEqn assamble = 0.000587 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000363 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001813 s +YEqn assamble = 0.000658 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000246 s +YEqn correct boundary = 0 s +EEqn Time = 0.000452 s +EEqn assamble = 0.000338 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 24.27 s ClockTime = 25 s +Courant Number mean: 0.000192325 max: 0.0175886 +Time = 0.0004475 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 47 new parcels + +Cloud: sprayCloud + Current number of parcels = 6668 + Current mass in system = 7.06246e-10 + Linear momentum = (2.7484e-11 -6.93165e-09 0) + |Linear momentum| = 6.9317e-09 + Linear kinetic energy = 3.59119e-08 + model1: + number of parcels added = 6673 + mass introduced = 7.14231e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.151, 506.88 + Mass transfer phase change = 7.98445e-12 + D10, D32, Dmax (mu) = 50.1579, 77.9258, 149.035 + Liquid penetration 95% mass (m) = 0.00368838 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00473512, Final residual = 5.90744e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0122621, Final residual = 3.48683e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00349088, Final residual = 2.83842e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00372081, Final residual = 1.69866e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00402555, Final residual = 2.11067e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00402557, Final residual = 2.11259e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00306394, Final residual = 1.84633e-07, No Iterations 1 +min/max(T) = 627.626, 835.195 +GAMG: Solving for p, Initial residual = 0.0455525, Final residual = 0.000650742, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.22779e-06, global = 1.20138e-06, cumulative = 0.000184171 +GAMG: Solving for p, Initial residual = 0.000635896, Final residual = 1.8417e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.19421e-06, global = 1.1942e-06, cumulative = 0.000185365 +smoothSolver: Solving for epsilon, Initial residual = 0.000955333, Final residual = 1.63227e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00509521, Final residual = 8.44446e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.07887 s +other Time = 0 s +rho Equations = 0.000136 s +U Equations = 0.000958 s +Y Equations = 0.00235187 s +E Equations = 0.000607 s +p Equations = 0.002471 s +calculate parcels = 9.07304 s +chemistry correctThermo = 0.002747 s +turbulence correct = 0.000973 s +combustion correct(in Y) = 0.0684591 s +percentage of chemistry = 86.8 % +percentage of rho/U/Y/E = 5.13868 % +========Time details of each equation======= +rhoEqn Time = 0.000286 s +rhoEqn assamble = 0.000226 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000957 s +UEqn assamble = 0.000583 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000374 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001769 s +YEqn assamble = 0.000633 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000202 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 24.48 s ClockTime = 25 s +Courant Number mean: 0.000192378 max: 0.0176214 +Time = 0.00045 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 6716 + Current mass in system = 7.10333e-10 + Linear momentum = (2.6968e-11 -6.96734e-09 0) + |Linear momentum| = 6.96739e-09 + Linear kinetic energy = 3.60807e-08 + model1: + number of parcels added = 6721 + mass introduced = 7.18421e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.153, 507.109 + Mass transfer phase change = 8.08899e-12 + D10, D32, Dmax (mu) = 50.2182, 77.9976, 149.04 + Liquid penetration 95% mass (m) = 0.00370745 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00454215, Final residual = 5.87274e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.01153, Final residual = 3.36467e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00346177, Final residual = 2.7831e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00370335, Final residual = 1.69101e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00400216, Final residual = 2.0963e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00400218, Final residual = 2.09819e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00305058, Final residual = 1.82276e-07, No Iterations 1 +min/max(T) = 627.803, 835.562 +GAMG: Solving for p, Initial residual = 0.0469496, Final residual = 0.000698039, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.24036e-06, global = 1.21372e-06, cumulative = 0.000186579 +GAMG: Solving for p, Initial residual = 0.00068144, Final residual = 9.22596e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.20494e-06, global = 1.20489e-06, cumulative = 0.000187784 +smoothSolver: Solving for epsilon, Initial residual = 0.000960715, Final residual = 1.64361e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00507051, Final residual = 8.41267e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.08874 s +other Time = 0 s +rho Equations = 0.000158 s +U Equations = 0.001125 s +Y Equations = 0.00238042 s +E Equations = 0.000628 s +p Equations = 0.002206 s +calculate parcels = 9.18451 s +chemistry correctThermo = 0.002746 s +turbulence correct = 0.000967 s +combustion correct(in Y) = 0.0783436 s +percentage of chemistry = 88.2844 % +percentage of rho/U/Y/E = 4.83595 % +========Time details of each equation======= +rhoEqn Time = 0.0003 s +rhoEqn assamble = 0.000234 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001125 s +UEqn assamble = 0.00069 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000435 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001725 s +YEqn assamble = 0.000662 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000177 s +YEqn correct boundary = 0 s +EEqn Time = 0.000472 s +EEqn assamble = 0.000356 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 24.68 s ClockTime = 25 s +Courant Number mean: 0.000192666 max: 0.0176609 +Time = 0.0004525 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 56 new parcels + +Cloud: sprayCloud + Current number of parcels = 6772 + Current mass in system = 7.1511e-10 + Linear momentum = (2.67007e-11 -7.01203e-09 0) + |Linear momentum| = 7.01208e-09 + Linear kinetic energy = 3.63089e-08 + model1: + number of parcels added = 6777 + mass introduced = 7.23305e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.153, 507.335 + Mass transfer phase change = 8.19453e-12 + D10, D32, Dmax (mu) = 50.3066, 78.0343, 149.046 + Liquid penetration 95% mass (m) = 0.0037268 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00455277, Final residual = 5.80036e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0108922, Final residual = 3.24862e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00344149, Final residual = 2.70398e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00368795, Final residual = 1.69111e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00398016, Final residual = 2.08044e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00398018, Final residual = 2.08232e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00304431, Final residual = 1.78258e-07, No Iterations 1 +min/max(T) = 627.964, 835.93 +GAMG: Solving for p, Initial residual = 0.0485413, Final residual = 0.000787862, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.2535e-06, global = 1.22377e-06, cumulative = 0.000189007 +GAMG: Solving for p, Initial residual = 0.000774119, Final residual = 2.04209e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.21646e-06, global = 1.21645e-06, cumulative = 0.000190224 +smoothSolver: Solving for epsilon, Initial residual = 0.00096567, Final residual = 1.65385e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00504526, Final residual = 8.37846e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.090149 s +other Time = 1e-06 s +rho Equations = 0.000163 s +U Equations = 0.001108 s +Y Equations = 0.00240832 s +E Equations = 0.000605 s +p Equations = 0.002365 s +calculate parcels = 9.31077 s +chemistry correctThermo = 0.002793 s +turbulence correct = 0.001004 s +combustion correct(in Y) = 0.0795057 s +percentage of chemistry = 88.1936 % +percentage of rho/U/Y/E = 4.75249 % +========Time details of each equation======= +rhoEqn Time = 0.000307 s +rhoEqn assamble = 0.000242 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001107 s +UEqn assamble = 0.000676 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000431 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00171 s +YEqn assamble = 0.000648 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000148 s +YEqn correct boundary = 0 s +EEqn Time = 0.000449 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 24.9 s ClockTime = 25 s +Courant Number mean: 0.000193118 max: 0.0176838 +Time = 0.000455 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 40 new parcels + +Cloud: sprayCloud + Current number of parcels = 6812 + Current mass in system = 7.185e-10 + Linear momentum = (2.52587e-11 -7.03852e-09 0) + |Linear momentum| = 7.03857e-09 + Linear kinetic energy = 3.64172e-08 + model1: + number of parcels added = 6817 + mass introduced = 7.26801e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.149, 507.558 + Mass transfer phase change = 8.30099e-12 + D10, D32, Dmax (mu) = 50.3686, 78.0579, 149.051 + Liquid penetration 95% mass (m) = 0.00374624 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00470443, Final residual = 5.72175e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0101608, Final residual = 3.06746e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00342541, Final residual = 2.58448e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00367096, Final residual = 1.68363e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00395728, Final residual = 2.06271e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0039573, Final residual = 2.06459e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00304539, Final residual = 1.77619e-07, No Iterations 1 +min/max(T) = 628.095, 836.297 +GAMG: Solving for p, Initial residual = 0.05052, Final residual = 0.000743246, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.26002e-06, global = 1.23462e-06, cumulative = 0.000191459 +GAMG: Solving for p, Initial residual = 0.000737287, Final residual = 5.83257e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.22718e-06, global = 1.22715e-06, cumulative = 0.000192686 +smoothSolver: Solving for epsilon, Initial residual = 0.00097088, Final residual = 1.66462e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00501983, Final residual = 8.34329e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.068917 s +other Time = 0 s +rho Equations = 0.000206 s +U Equations = 0.001109 s +Y Equations = 0.00244501 s +E Equations = 0.000501 s +p Equations = 0.001859 s +calculate parcels = 9.42 s +chemistry correctThermo = 0.00187 s +turbulence correct = 0.00092 s +combustion correct(in Y) = 0.059794 s +percentage of chemistry = 86.7623 % +percentage of rho/U/Y/E = 6.18282 % +========Time details of each equation======= +rhoEqn Time = 0.000327 s +rhoEqn assamble = 0.000265 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001108 s +UEqn assamble = 0.000689 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000419 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001742 s +YEqn assamble = 0.000798 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 6.6e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000374 s +EEqn assamble = 0.000282 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 25.08 s ClockTime = 25 s +Courant Number mean: 0.000193649 max: 0.0177315 +Time = 0.0004575 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 52 new parcels + +Cloud: sprayCloud + Current number of parcels = 6864 + Current mass in system = 7.22916e-10 + Linear momentum = (2.57062e-11 -7.07847e-09 0) + |Linear momentum| = 7.07852e-09 + Linear kinetic energy = 3.6614e-08 + model1: + number of parcels added = 6869 + mass introduced = 7.31324e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.139, 507.777 + Mass transfer phase change = 8.4084e-12 + D10, D32, Dmax (mu) = 50.434, 78.0829, 149.057 + Liquid penetration 95% mass (m) = 0.00376474 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00460933, Final residual = 5.73999e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00948851, Final residual = 2.93067e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00340158, Final residual = 2.4605e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00365451, Final residual = 1.67771e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00393538, Final residual = 2.04597e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0039354, Final residual = 2.04783e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00304709, Final residual = 1.79291e-07, No Iterations 1 +min/max(T) = 628.211, 836.668 +GAMG: Solving for p, Initial residual = 0.0510174, Final residual = 0.000639685, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.2661e-06, global = 1.24523e-06, cumulative = 0.000193931 +GAMG: Solving for p, Initial residual = 0.000633938, Final residual = 6.45948e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.23799e-06, global = 1.23796e-06, cumulative = 0.000195169 +smoothSolver: Solving for epsilon, Initial residual = 0.000975843, Final residual = 1.6753e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00499332, Final residual = 8.30567e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.068537 s +other Time = 0 s +rho Equations = 0.000155 s +U Equations = 0.00098 s +Y Equations = 0.00215734 s +E Equations = 0.000502 s +p Equations = 0.001889 s +calculate parcels = 9.51029 s +chemistry correctThermo = 0.002032 s +turbulence correct = 0.000852 s +combustion correct(in Y) = 0.0597837 s +percentage of chemistry = 87.2283 % +percentage of rho/U/Y/E = 5.53618 % +========Time details of each equation======= +rhoEqn Time = 0.000281 s +rhoEqn assamble = 0.000225 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000979 s +UEqn assamble = 0.000624 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000355 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001598 s +YEqn assamble = 0.000557 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000197 s +YEqn correct boundary = 0 s +EEqn Time = 0.000374 s +EEqn assamble = 0.000279 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 25.23 s ClockTime = 26 s +Courant Number mean: 0.000194307 max: 0.017803 +Time = 0.00046 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 6912 + Current mass in system = 7.26986e-10 + Linear momentum = (2.58077e-11 -7.11398e-09 0) + |Linear momentum| = 7.11403e-09 + Linear kinetic energy = 3.67813e-08 + model1: + number of parcels added = 6917 + mass introduced = 7.35503e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.167, 507.994 + Mass transfer phase change = 8.51663e-12 + D10, D32, Dmax (mu) = 50.4935, 78.145, 149.15 + Liquid penetration 95% mass (m) = 0.00378351 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00450406, Final residual = 5.86145e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00880865, Final residual = 2.73649e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00339379, Final residual = 2.49172e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0036357, Final residual = 1.66444e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00391346, Final residual = 2.03515e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00391348, Final residual = 2.03699e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00303114, Final residual = 1.80541e-07, No Iterations 1 +min/max(T) = 628.332, 837.039 +GAMG: Solving for p, Initial residual = 0.0543214, Final residual = 0.000810089, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.28441e-06, global = 1.2514e-06, cumulative = 0.00019642 +GAMG: Solving for p, Initial residual = 0.000795948, Final residual = 1.77703e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.24747e-06, global = 1.24746e-06, cumulative = 0.000197668 +smoothSolver: Solving for epsilon, Initial residual = 0.000980831, Final residual = 1.68533e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00496719, Final residual = 8.2665e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.089271 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001177 s +Y Equations = 0.00245388 s +E Equations = 0.000636 s +p Equations = 0.002507 s +calculate parcels = 9.59938 s +chemistry correctThermo = 0.002775 s +turbulence correct = 0.001117 s +combustion correct(in Y) = 0.0782241 s +percentage of chemistry = 87.6255 % +percentage of rho/U/Y/E = 4.97796 % +========Time details of each equation======= +rhoEqn Time = 0.000341 s +rhoEqn assamble = 0.000273 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001176 s +UEqn assamble = 0.000714 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000462 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001776 s +YEqn assamble = 0.000678 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000164 s +YEqn correct boundary = 0 s +EEqn Time = 0.000465 s +EEqn assamble = 0.000348 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 25.41 s ClockTime = 26 s +Courant Number mean: 0.000195062 max: 0.0178293 +Time = 0.0004625 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 6958 + Current mass in system = 7.30878e-10 + Linear momentum = (2.59418e-11 -7.14713e-09 0) + |Linear momentum| = 7.14718e-09 + Linear kinetic energy = 3.69334e-08 + model1: + number of parcels added = 6963 + mass introduced = 7.39504e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.145, 508.207 + Mass transfer phase change = 8.62573e-12 + D10, D32, Dmax (mu) = 50.5502, 78.1815, 149.068 + Liquid penetration 95% mass (m) = 0.00380275 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00417136, Final residual = 5.69858e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00853989, Final residual = 2.70604e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00338033, Final residual = 2.45936e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00361736, Final residual = 1.65658e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00389183, Final residual = 2.02322e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00389185, Final residual = 2.02504e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00301443, Final residual = 1.79932e-07, No Iterations 1 +min/max(T) = 628.44, 837.412 +GAMG: Solving for p, Initial residual = 0.0540123, Final residual = 0.000753946, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.29268e-06, global = 1.26337e-06, cumulative = 0.000198931 +GAMG: Solving for p, Initial residual = 0.000745749, Final residual = 9.23927e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.2575e-06, global = 1.25746e-06, cumulative = 0.000200189 +smoothSolver: Solving for epsilon, Initial residual = 0.000985794, Final residual = 1.69493e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00494126, Final residual = 8.22625e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095251 s +other Time = 0 s +rho Equations = 0.000166 s +U Equations = 0.00117 s +Y Equations = 0.00246292 s +E Equations = 0.000619 s +p Equations = 0.002246 s +calculate parcels = 9.7129 s +chemistry correctThermo = 0.002791 s +turbulence correct = 0.000996 s +combustion correct(in Y) = 0.0846021 s +percentage of chemistry = 88.8201 % +percentage of rho/U/Y/E = 4.63819 % +========Time details of each equation======= +rhoEqn Time = 0.00031 s +rhoEqn assamble = 0.000242 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00117 s +UEqn assamble = 0.000711 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000459 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001811 s +YEqn assamble = 0.000673 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000206 s +YEqn correct boundary = 0 s +EEqn Time = 0.000459 s +EEqn assamble = 0.000343 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 25.62 s ClockTime = 26 s +Courant Number mean: 0.00019593 max: 0.0178699 +Time = 0.000465 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 38 new parcels + +Cloud: sprayCloud + Current number of parcels = 6996 + Current mass in system = 7.34069e-10 + Linear momentum = (2.52082e-11 -7.17107e-09 0) + |Linear momentum| = 7.17112e-09 + Linear kinetic energy = 3.70248e-08 + model1: + number of parcels added = 7001 + mass introduced = 7.42804e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.173, 508.391 + Mass transfer phase change = 8.73578e-12 + D10, D32, Dmax (mu) = 50.5311, 78.1468, 149.073 + Liquid penetration 95% mass (m) = 0.00382137 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00425766, Final residual = 6.06262e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00875493, Final residual = 2.72701e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00335549, Final residual = 2.39593e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00359961, Final residual = 1.64628e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00387005, Final residual = 2.01021e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00387007, Final residual = 2.01201e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00298959, Final residual = 1.81028e-07, No Iterations 1 +min/max(T) = 628.549, 837.785 +GAMG: Solving for p, Initial residual = 0.0543905, Final residual = 0.000764822, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.3018e-06, global = 1.27766e-06, cumulative = 0.000201466 +GAMG: Solving for p, Initial residual = 0.000752291, Final residual = 8.14708e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.26852e-06, global = 1.26848e-06, cumulative = 0.000202735 +smoothSolver: Solving for epsilon, Initial residual = 0.000990197, Final residual = 1.70363e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00491505, Final residual = 8.18497e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095377 s +other Time = 0 s +rho Equations = 0.000158 s +U Equations = 0.001157 s +Y Equations = 0.00237374 s +E Equations = 0.000605 s +p Equations = 0.002268 s +calculate parcels = 9.83564 s +chemistry correctThermo = 0.00288 s +turbulence correct = 0.000994 s +combustion correct(in Y) = 0.0847473 s +percentage of chemistry = 88.855 % +percentage of rho/U/Y/E = 4.50186 % +========Time details of each equation======= +rhoEqn Time = 0.000305 s +rhoEqn assamble = 0.000239 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001156 s +UEqn assamble = 0.000719 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000437 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001736 s +YEqn assamble = 0.000649 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000178 s +YEqn correct boundary = 0 s +EEqn Time = 0.000448 s +EEqn assamble = 0.000333 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 25.84 s ClockTime = 26 s +Courant Number mean: 0.000196962 max: 0.0179012 +Time = 0.0004675 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 7040 + Current mass in system = 7.3776e-10 + Linear momentum = (2.44097e-11 -7.20153e-09 0) + |Linear momentum| = 7.20157e-09 + Linear kinetic energy = 3.71596e-08 + model1: + number of parcels added = 7045 + mass introduced = 7.46607e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.161, 508.544 + Mass transfer phase change = 8.84678e-12 + D10, D32, Dmax (mu) = 50.5055, 78.1375, 149.079 + Liquid penetration 95% mass (m) = 0.00384159 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00472455, Final residual = 6.5339e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00899724, Final residual = 2.692e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00335207, Final residual = 2.32548e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00358247, Final residual = 1.63494e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00384937, Final residual = 1.99571e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00384939, Final residual = 1.99749e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00297803, Final residual = 1.81896e-07, No Iterations 1 +min/max(T) = 628.648, 838.158 +GAMG: Solving for p, Initial residual = 0.0553537, Final residual = 0.000788274, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.30981e-06, global = 1.28547e-06, cumulative = 0.00020402 +GAMG: Solving for p, Initial residual = 0.000779686, Final residual = 7.51608e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.27933e-06, global = 1.2793e-06, cumulative = 0.000205299 +smoothSolver: Solving for epsilon, Initial residual = 0.000994841, Final residual = 1.7126e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00488998, Final residual = 8.14467e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.091322 s +other Time = 0 s +rho Equations = 0.000165 s +U Equations = 0.001125 s +Y Equations = 0.00240315 s +E Equations = 0.000647 s +p Equations = 0.002207 s +calculate parcels = 9.95549 s +chemistry correctThermo = 0.002777 s +turbulence correct = 0.001173 s +combustion correct(in Y) = 0.0806218 s +percentage of chemistry = 88.2831 % +percentage of rho/U/Y/E = 4.75258 % +========Time details of each equation======= +rhoEqn Time = 0.000305 s +rhoEqn assamble = 0.000241 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001125 s +UEqn assamble = 0.000677 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000448 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001738 s +YEqn assamble = 0.000651 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000167 s +YEqn correct boundary = 0 s +EEqn Time = 0.000492 s +EEqn assamble = 0.000371 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000121 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 26.05 s ClockTime = 26 s +Courant Number mean: 0.000198053 max: 0.0179326 +Time = 0.00047 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 55 new parcels + +Cloud: sprayCloud + Current number of parcels = 7095 + Current mass in system = 7.42389e-10 + Linear momentum = (2.36984e-11 -7.24423e-09 0) + |Linear momentum| = 7.24427e-09 + Linear kinetic energy = 3.73754e-08 + model1: + number of parcels added = 7100 + mass introduced = 7.51348e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.145, 508.689 + Mass transfer phase change = 8.95869e-12 + D10, D32, Dmax (mu) = 50.5586, 78.168, 149.267 + Liquid penetration 95% mass (m) = 0.00386209 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00494714, Final residual = 6.75655e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00926431, Final residual = 2.72958e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00333345, Final residual = 2.25253e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00356539, Final residual = 1.62825e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00382824, Final residual = 1.98457e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00382826, Final residual = 1.98636e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00295429, Final residual = 1.80457e-07, No Iterations 1 +min/max(T) = 628.707, 838.533 +GAMG: Solving for p, Initial residual = 0.056149, Final residual = 0.000727949, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.31678e-06, global = 1.2948e-06, cumulative = 0.000206594 +GAMG: Solving for p, Initial residual = 0.000719997, Final residual = 6.5976e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.28999e-06, global = 1.28997e-06, cumulative = 0.000207884 +smoothSolver: Solving for epsilon, Initial residual = 0.000999173, Final residual = 1.72057e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00486475, Final residual = 8.10277e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.084256 s +other Time = 0 s +rho Equations = 0.000166 s +U Equations = 0.00114 s +Y Equations = 0.00208967 s +E Equations = 0.00049 s +p Equations = 0.001821 s +calculate parcels = 10.0812 s +chemistry correctThermo = 0.002021 s +turbulence correct = 0.00082 s +combustion correct(in Y) = 0.0755193 s +percentage of chemistry = 89.6308 % +percentage of rho/U/Y/E = 4.61174 % +========Time details of each equation======= +rhoEqn Time = 0.000282 s +rhoEqn assamble = 0.000223 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001139 s +UEqn assamble = 0.000682 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000457 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00139 s +YEqn assamble = 0.000547 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 6.4e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000371 s +EEqn assamble = 0.000276 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 26.26 s ClockTime = 27 s +Courant Number mean: 0.000199216 max: 0.0179462 +Time = 0.0004725 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 7146 + Current mass in system = 7.46683e-10 + Linear momentum = (2.37937e-11 -7.28251e-09 0) + |Linear momentum| = 7.28254e-09 + Linear kinetic energy = 3.75621e-08 + model1: + number of parcels added = 7151 + mass introduced = 7.55754e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.143, 508.826 + Mass transfer phase change = 9.07152e-12 + D10, D32, Dmax (mu) = 50.6245, 78.2196, 149.102 + Liquid penetration 95% mass (m) = 0.00388036 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00499195, Final residual = 6.89092e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00951969, Final residual = 2.77121e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0033319, Final residual = 2.24052e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0035478, Final residual = 1.61581e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00380716, Final residual = 1.97466e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00380718, Final residual = 1.97644e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00294114, Final residual = 1.81799e-07, No Iterations 1 +min/max(T) = 628.744, 838.909 +GAMG: Solving for p, Initial residual = 0.0566975, Final residual = 0.000798571, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.33031e-06, global = 1.30727e-06, cumulative = 0.000209191 +GAMG: Solving for p, Initial residual = 0.000791566, Final residual = 8.09349e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.30048e-06, global = 1.30044e-06, cumulative = 0.000210492 +smoothSolver: Solving for epsilon, Initial residual = 0.00100366, Final residual = 1.72869e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00484036, Final residual = 8.06172e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094871 s +other Time = 0 s +rho Equations = 0.000168 s +U Equations = 0.001122 s +Y Equations = 0.00244186 s +E Equations = 0.000605 s +p Equations = 0.002211 s +calculate parcels = 10.2106 s +chemistry correctThermo = 0.002779 s +turbulence correct = 0.001071 s +combustion correct(in Y) = 0.0842751 s +percentage of chemistry = 88.8313 % +percentage of rho/U/Y/E = 4.57132 % +========Time details of each equation======= +rhoEqn Time = 0.000315 s +rhoEqn assamble = 0.000252 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001119 s +UEqn assamble = 0.000683 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000436 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.0018 s +YEqn assamble = 0.000675 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000221 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 26.49 s ClockTime = 27 s +Courant Number mean: 0.00020041 max: 0.0179739 +Time = 0.000475 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 54 new parcels + +Cloud: sprayCloud + Current number of parcels = 7200 + Current mass in system = 7.51237e-10 + Linear momentum = (2.55805e-11 -7.32428e-09 0) + |Linear momentum| = 7.32432e-09 + Linear kinetic energy = 3.77715e-08 + model1: + number of parcels added = 7205 + mass introduced = 7.60423e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.183, 508.956 + Mass transfer phase change = 9.18523e-12 + D10, D32, Dmax (mu) = 50.7023, 78.2759, 149.095 + Liquid penetration 95% mass (m) = 0.00389932 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00485262, Final residual = 6.69411e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00981016, Final residual = 2.85355e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00331656, Final residual = 2.19916e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00353013, Final residual = 1.60495e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00378631, Final residual = 1.96397e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00378633, Final residual = 1.96573e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00291846, Final residual = 1.82242e-07, No Iterations 1 +min/max(T) = 628.774, 839.287 +GAMG: Solving for p, Initial residual = 0.0567764, Final residual = 0.000643331, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.33511e-06, global = 1.3161e-06, cumulative = 0.000211808 +GAMG: Solving for p, Initial residual = 0.000635164, Final residual = 6.1475e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.31059e-06, global = 1.31056e-06, cumulative = 0.000213119 +smoothSolver: Solving for epsilon, Initial residual = 0.00100783, Final residual = 1.73611e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00481616, Final residual = 8.02009e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.076752 s +other Time = 0 s +rho Equations = 0.000147 s +U Equations = 0.000911 s +Y Equations = 0.00267389 s +E Equations = 0.00069 s +p Equations = 0.001933 s +calculate parcels = 10.3401 s +chemistry correctThermo = 0.002622 s +turbulence correct = 0.000864 s +combustion correct(in Y) = 0.0667381 s +percentage of chemistry = 86.9529 % +percentage of rho/U/Y/E = 5.76127 % +========Time details of each equation======= +rhoEqn Time = 0.000277 s +rhoEqn assamble = 0.000212 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00091 s +UEqn assamble = 0.000561 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000349 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002128 s +YEqn assamble = 0.000739 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000307 s +YEqn correct boundary = 0 s +EEqn Time = 0.000511 s +EEqn assamble = 0.000375 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000136 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 26.69 s ClockTime = 27 s +Courant Number mean: 0.000201643 max: 0.0180047 +Time = 0.0004775 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 55 new parcels + +Cloud: sprayCloud + Current number of parcels = 7255 + Current mass in system = 7.55886e-10 + Linear momentum = (2.67246e-11 -7.36724e-09 0) + |Linear momentum| = 7.36729e-09 + Linear kinetic energy = 3.7989e-08 + model1: + number of parcels added = 7260 + mass introduced = 7.65186e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.15, 509.078 + Mass transfer phase change = 9.29982e-12 + D10, D32, Dmax (mu) = 50.7588, 78.3272, 149.101 + Liquid penetration 95% mass (m) = 0.00391829 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00464877, Final residual = 6.38426e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00997818, Final residual = 2.90224e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00329606, Final residual = 2.21849e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0035124, Final residual = 1.59295e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00376542, Final residual = 1.95269e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00376544, Final residual = 1.95443e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00290329, Final residual = 1.83353e-07, No Iterations 1 +min/max(T) = 628.809, 839.666 +GAMG: Solving for p, Initial residual = 0.0578075, Final residual = 0.000654318, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.34635e-06, global = 1.32359e-06, cumulative = 0.000214442 +GAMG: Solving for p, Initial residual = 0.000645496, Final residual = 6.55166e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.32083e-06, global = 1.32081e-06, cumulative = 0.000215763 +smoothSolver: Solving for epsilon, Initial residual = 0.00101197, Final residual = 1.74331e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00479198, Final residual = 7.97776e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.091258 s +other Time = 0 s +rho Equations = 0.000169 s +U Equations = 0.001131 s +Y Equations = 0.00233316 s +E Equations = 0.000614 s +p Equations = 0.002328 s +calculate parcels = 10.4904 s +chemistry correctThermo = 0.002802 s +turbulence correct = 0.000973 s +combustion correct(in Y) = 0.0807128 s +percentage of chemistry = 88.4447 % +percentage of rho/U/Y/E = 4.65401 % +========Time details of each equation======= +rhoEqn Time = 0.000323 s +rhoEqn assamble = 0.000254 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001129 s +UEqn assamble = 0.000695 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000434 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001678 s +YEqn assamble = 0.000638 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000169 s +YEqn correct boundary = 0 s +EEqn Time = 0.000458 s +EEqn assamble = 0.000344 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 26.93 s ClockTime = 27 s +Courant Number mean: 0.000202957 max: 0.0180392 +Time = 0.00048 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 7299 + Current mass in system = 7.5959e-10 + Linear momentum = (2.78026e-11 -7.39783e-09 0) + |Linear momentum| = 7.39788e-09 + Linear kinetic energy = 3.81248e-08 + model1: + number of parcels added = 7304 + mass introduced = 7.69005e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.153, 509.193 + Mass transfer phase change = 9.41522e-12 + D10, D32, Dmax (mu) = 50.8021, 78.3663, 149.107 + Liquid penetration 95% mass (m) = 0.00393741 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00446549, Final residual = 6.32858e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0100474, Final residual = 2.91143e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0032776, Final residual = 2.23335e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00349371, Final residual = 1.58246e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00374542, Final residual = 1.94631e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00374544, Final residual = 1.94804e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00288586, Final residual = 1.8387e-07, No Iterations 1 +min/max(T) = 628.829, 840.045 +GAMG: Solving for p, Initial residual = 0.0584013, Final residual = 0.000668409, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.35565e-06, global = 1.33258e-06, cumulative = 0.000217096 +GAMG: Solving for p, Initial residual = 0.000664197, Final residual = 9.52008e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.33017e-06, global = 1.33013e-06, cumulative = 0.000218426 +smoothSolver: Solving for epsilon, Initial residual = 0.00101629, Final residual = 1.75046e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00476816, Final residual = 7.93592e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.082723 s +other Time = 0 s +rho Equations = 0.00017 s +U Equations = 0.00115 s +Y Equations = 0.00225805 s +E Equations = 0.0005 s +p Equations = 0.001802 s +calculate parcels = 10.621 s +chemistry correctThermo = 0.001988 s +turbulence correct = 0.000939 s +combustion correct(in Y) = 0.073719 s +percentage of chemistry = 89.1154 % +percentage of rho/U/Y/E = 4.92976 % +========Time details of each equation======= +rhoEqn Time = 0.000289 s +rhoEqn assamble = 0.000226 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00115 s +UEqn assamble = 0.000692 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000458 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001601 s +YEqn assamble = 0.000629 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000102 s +YEqn correct boundary = 0 s +EEqn Time = 0.000378 s +EEqn assamble = 0.000285 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 27.15 s ClockTime = 28 s +Courant Number mean: 0.000204343 max: 0.0180703 +Time = 0.0004825 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 52 new parcels + +Cloud: sprayCloud + Current number of parcels = 7351 + Current mass in system = 7.63977e-10 + Linear momentum = (2.93444e-11 -7.4373e-09 0) + |Linear momentum| = 7.43736e-09 + Linear kinetic energy = 3.83194e-08 + model1: + number of parcels added = 7356 + mass introduced = 7.73508e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.155, 509.301 + Mass transfer phase change = 9.53154e-12 + D10, D32, Dmax (mu) = 50.8209, 78.374, 149.112 + Liquid penetration 95% mass (m) = 0.00395508 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00427037, Final residual = 6.27717e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0100689, Final residual = 2.92292e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00326849, Final residual = 2.23579e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00347591, Final residual = 1.57291e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00372503, Final residual = 1.94255e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00372505, Final residual = 1.94427e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00285966, Final residual = 1.84847e-07, No Iterations 1 +min/max(T) = 628.824, 840.426 +GAMG: Solving for p, Initial residual = 0.0590699, Final residual = 0.000731424, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.36464e-06, global = 1.34306e-06, cumulative = 0.000219769 +GAMG: Solving for p, Initial residual = 0.000734575, Final residual = 1.6317e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.34066e-06, global = 1.34065e-06, cumulative = 0.000221109 +smoothSolver: Solving for epsilon, Initial residual = 0.00102024, Final residual = 1.75696e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00474451, Final residual = 7.89401e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.089791 s +other Time = 0 s +rho Equations = 0.000254 s +U Equations = 0.001574 s +Y Equations = 0.00266642 s +E Equations = 0.000617 s +p Equations = 0.003003 s +calculate parcels = 10.7431 s +chemistry correctThermo = 0.002812 s +turbulence correct = 0.001125 s +combustion correct(in Y) = 0.0774126 s +percentage of chemistry = 86.2142 % +percentage of rho/U/Y/E = 5.69258 % +========Time details of each equation======= +rhoEqn Time = 0.000432 s +rhoEqn assamble = 0.000332 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.0001 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001573 s +UEqn assamble = 0.0009 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000673 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001586 s +YEqn assamble = 0.000659 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -3.9e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000459 s +EEqn assamble = 0.000344 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 27.36 s ClockTime = 28 s +Courant Number mean: 0.00020583 max: 0.0180937 +Time = 0.000485 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 59 new parcels + +Cloud: sprayCloud + Current number of parcels = 7410 + Current mass in system = 7.68973e-10 + Linear momentum = (2.91416e-11 -7.48451e-09 0) + |Linear momentum| = 7.48457e-09 + Linear kinetic energy = 3.85644e-08 + model1: + number of parcels added = 7415 + mass introduced = 7.78622e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.149, 509.403 + Mass transfer phase change = 9.64915e-12 + D10, D32, Dmax (mu) = 44.5212, 78.2609, 149.118 + Liquid penetration 95% mass (m) = 0.00397379 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00429199, Final residual = 6.33418e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0100151, Final residual = 2.90798e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00325308, Final residual = 2.17832e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00346311, Final residual = 1.58451e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00370533, Final residual = 1.93726e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00370535, Final residual = 1.93897e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0028446, Final residual = 1.86943e-07, No Iterations 1 +min/max(T) = 628.793, 840.806 +GAMG: Solving for p, Initial residual = 0.0624477, Final residual = 0.00178807, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.41296e-06, global = 1.37684e-06, cumulative = 0.000222486 +GAMG: Solving for p, Initial residual = 0.00183468, Final residual = 7.22853e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.35565e-06, global = 1.35563e-06, cumulative = 0.000223842 +smoothSolver: Solving for epsilon, Initial residual = 0.00102242, Final residual = 1.76042e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00471819, Final residual = 7.8447e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.070117 s +other Time = 0 s +rho Equations = 0.000158 s +U Equations = 0.001238 s +Y Equations = 0.0020381 s +E Equations = 0.000553 s +p Equations = 0.002053 s +calculate parcels = 10.8475 s +chemistry correctThermo = 0.002012 s +turbulence correct = 0.000829 s +combustion correct(in Y) = 0.0610529 s +percentage of chemistry = 87.0729 % +percentage of rho/U/Y/E = 5.68636 % +========Time details of each equation======= +rhoEqn Time = 0.000278 s +rhoEqn assamble = 0.000221 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001236 s +UEqn assamble = 0.000839 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000397 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001443 s +YEqn assamble = 0.00053 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00011 s +YEqn correct boundary = 0 s +EEqn Time = 0.000393 s +EEqn assamble = 0.000299 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 27.53 s ClockTime = 28 s +Courant Number mean: 0.000207614 max: 0.0181256 +Time = 0.0004875 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 7461 + Current mass in system = 7.73293e-10 + Linear momentum = (2.96252e-11 -7.52285e-09 0) + |Linear momentum| = 7.5229e-09 + Linear kinetic energy = 3.87513e-08 + model1: + number of parcels added = 7466 + mass introduced = 7.83061e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.161, 509.498 + Mass transfer phase change = 9.76789e-12 + D10, D32, Dmax (mu) = 44.5974, 78.3405, 149.324 + Liquid penetration 95% mass (m) = 0.00399206 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00511482, Final residual = 7.14983e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00973367, Final residual = 2.65457e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00322653, Final residual = 2.15351e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00344577, Final residual = 1.58741e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00368381, Final residual = 1.9305e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00368383, Final residual = 1.93221e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00282128, Final residual = 1.84412e-07, No Iterations 1 +min/max(T) = 628.761, 841.178 +GAMG: Solving for p, Initial residual = 0.0686695, Final residual = 0.0013147, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.40764e-06, global = 1.37378e-06, cumulative = 0.000225216 +GAMG: Solving for p, Initial residual = 0.00134512, Final residual = 5.45488e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.36852e-06, global = 1.3685e-06, cumulative = 0.000226584 +smoothSolver: Solving for epsilon, Initial residual = 0.00102602, Final residual = 1.76618e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00469414, Final residual = 7.80156e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.066873 s +other Time = 0 s +rho Equations = 0.000157 s +U Equations = 0.001009 s +Y Equations = 0.00206079 s +E Equations = 0.00049 s +p Equations = 0.001969 s +calculate parcels = 10.9452 s +chemistry correctThermo = 0.001937 s +turbulence correct = 0.000866 s +combustion correct(in Y) = 0.0582032 s +percentage of chemistry = 87.0354 % +percentage of rho/U/Y/E = 5.55798 % +========Time details of each equation======= +rhoEqn Time = 0.000278 s +rhoEqn assamble = 0.000218 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001009 s +UEqn assamble = 0.000622 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000387 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001474 s +YEqn assamble = 0.000542 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000114 s +YEqn correct boundary = 0 s +EEqn Time = 0.000369 s +EEqn assamble = 0.000275 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 27.7 s ClockTime = 28 s +Courant Number mean: 0.000209472 max: 0.0181525 +Time = 0.00049 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 7511 + Current mass in system = 7.77526e-10 + Linear momentum = (3.11986e-11 -7.56013e-09 0) + |Linear momentum| = 7.56019e-09 + Linear kinetic energy = 3.89304e-08 + model1: + number of parcels added = 7516 + mass introduced = 7.87414e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.153, 509.589 + Mass transfer phase change = 9.88797e-12 + D10, D32, Dmax (mu) = 44.6243, 78.3169, 149.129 + Liquid penetration 95% mass (m) = 0.0040109 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00507568, Final residual = 7.30219e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00946692, Final residual = 2.60434e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00319421, Final residual = 2.12308e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00343316, Final residual = 1.59482e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00366459, Final residual = 1.9219e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00366462, Final residual = 1.92359e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00280538, Final residual = 1.85304e-07, No Iterations 1 +min/max(T) = 628.705, 841.559 +GAMG: Solving for p, Initial residual = 0.0687764, Final residual = 0.000920494, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.41418e-06, global = 1.38884e-06, cumulative = 0.000227973 +GAMG: Solving for p, Initial residual = 0.000932869, Final residual = 3.97259e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.38407e-06, global = 1.38406e-06, cumulative = 0.000229357 +smoothSolver: Solving for epsilon, Initial residual = 0.00102974, Final residual = 1.77208e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00467094, Final residual = 7.76083e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.093713 s +other Time = 0 s +rho Equations = 0.000156 s +U Equations = 0.001099 s +Y Equations = 0.00207368 s +E Equations = 0.000502 s +p Equations = 0.002716 s +calculate parcels = 11.0616 s +chemistry correctThermo = 0.002071 s +turbulence correct = 0.001086 s +combustion correct(in Y) = 0.0836473 s +percentage of chemistry = 89.259 % +percentage of rho/U/Y/E = 4.08767 % +========Time details of each equation======= +rhoEqn Time = 0.000344 s +rhoEqn assamble = 0.000271 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001099 s +UEqn assamble = 0.000671 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000428 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001438 s +YEqn assamble = 0.000538 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000112 s +YEqn correct boundary = 0 s +EEqn Time = 0.000381 s +EEqn assamble = 0.000284 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.7e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 27.91 s ClockTime = 28 s +Courant Number mean: 0.000211404 max: 0.0181882 +Time = 0.0004925 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 52 new parcels + +Cloud: sprayCloud + Current number of parcels = 7563 + Current mass in system = 7.81933e-10 + Linear momentum = (3.14346e-11 -7.59959e-09 0) + |Linear momentum| = 7.59966e-09 + Linear kinetic energy = 3.91241e-08 + model1: + number of parcels added = 7568 + mass introduced = 7.91943e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.152, 509.676 + Mass transfer phase change = 1.00095e-11 + D10, D32, Dmax (mu) = 44.6307, 78.3211, 149.134 + Liquid penetration 95% mass (m) = 0.0040286 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00509333, Final residual = 7.36774e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00920225, Final residual = 2.56441e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00316439, Final residual = 2.13077e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00342013, Final residual = 1.60557e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00364435, Final residual = 1.91275e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00364437, Final residual = 1.91443e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00278989, Final residual = 1.86596e-07, No Iterations 1 +min/max(T) = 628.602, 841.94 +GAMG: Solving for p, Initial residual = 0.0734467, Final residual = 0.000974771, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.42833e-06, global = 1.40381e-06, cumulative = 0.000230761 +GAMG: Solving for p, Initial residual = 0.00100045, Final residual = 2.32203e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.40022e-06, global = 1.40021e-06, cumulative = 0.000232161 +smoothSolver: Solving for epsilon, Initial residual = 0.00103336, Final residual = 1.77763e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00464822, Final residual = 7.72093e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095359 s +other Time = 0 s +rho Equations = 0.000174 s +U Equations = 0.001148 s +Y Equations = 0.00249139 s +E Equations = 0.000639 s +p Equations = 0.002015 s +calculate parcels = 11.2013 s +chemistry correctThermo = 0.002178 s +turbulence correct = 0.000836 s +combustion correct(in Y) = 0.0856576 s +percentage of chemistry = 89.8265 % +percentage of rho/U/Y/E = 4.66908 % +========Time details of each equation======= +rhoEqn Time = 0.000319 s +rhoEqn assamble = 0.000251 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001148 s +UEqn assamble = 0.000706 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000442 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001816 s +YEqn assamble = 0.000684 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000188 s +YEqn correct boundary = 0 s +EEqn Time = 0.000461 s +EEqn assamble = 0.000343 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 28.14 s ClockTime = 29 s +Courant Number mean: 0.000213361 max: 0.0182096 +Time = 0.000495 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 53 new parcels + +Cloud: sprayCloud + Current number of parcels = 7616 + Current mass in system = 7.8643e-10 + Linear momentum = (3.08826e-11 -7.64032e-09 0) + |Linear momentum| = 7.64038e-09 + Linear kinetic energy = 3.93257e-08 + model1: + number of parcels added = 7621 + mass introduced = 7.96563e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.146, 509.757 + Mass transfer phase change = 1.01323e-11 + D10, D32, Dmax (mu) = 44.698, 78.3757, 149.14 + Liquid penetration 95% mass (m) = 0.00405025 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00498181, Final residual = 7.15809e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00880758, Final residual = 2.50256e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00315952, Final residual = 2.18057e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00340731, Final residual = 1.61671e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00362528, Final residual = 1.90185e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0036253, Final residual = 1.90351e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00277093, Final residual = 1.87917e-07, No Iterations 1 +min/max(T) = 628.3, 842.32 +GAMG: Solving for p, Initial residual = 0.0798586, Final residual = 0.0010868, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.446e-06, global = 1.42173e-06, cumulative = 0.000233583 +GAMG: Solving for p, Initial residual = 0.00112789, Final residual = 2.03253e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.41583e-06, global = 1.41582e-06, cumulative = 0.000234999 +smoothSolver: Solving for epsilon, Initial residual = 0.00103713, Final residual = 1.78354e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00462598, Final residual = 7.68249e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.082095 s +other Time = 0 s +rho Equations = 0.000137 s +U Equations = 0.00092 s +Y Equations = 0.00232427 s +E Equations = 0.000514 s +p Equations = 0.002031 s +calculate parcels = 11.3304 s +chemistry correctThermo = 0.002018 s +turbulence correct = 0.000833 s +combustion correct(in Y) = 0.0731517 s +percentage of chemistry = 89.1062 % +percentage of rho/U/Y/E = 4.74483 % +========Time details of each equation======= +rhoEqn Time = 0.000261 s +rhoEqn assamble = 0.000207 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00092 s +UEqn assamble = 0.000558 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000362 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001769 s +YEqn assamble = 0.00064 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000214 s +YEqn correct boundary = 0 s +EEqn Time = 0.000394 s +EEqn assamble = 0.000282 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 28.36 s ClockTime = 29 s +Courant Number mean: 0.000215289 max: 0.0182347 +Time = 0.0004975 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 43 new parcels + +Cloud: sprayCloud + Current number of parcels = 7659 + Current mass in system = 7.9006e-10 + Linear momentum = (3.08911e-11 -7.66965e-09 0) + |Linear momentum| = 7.66972e-09 + Linear kinetic energy = 3.94527e-08 + model1: + number of parcels added = 7664 + mass introduced = 8.00316e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.151, 509.834 + Mass transfer phase change = 1.02564e-11 + D10, D32, Dmax (mu) = 44.7603, 78.4118, 149.146 + Liquid penetration 95% mass (m) = 0.00406948 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00477154, Final residual = 7.10934e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00827808, Final residual = 2.40973e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00316042, Final residual = 2.22955e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00339337, Final residual = 1.62187e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00360624, Final residual = 1.89448e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00360626, Final residual = 1.89622e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00274642, Final residual = 1.87419e-07, No Iterations 1 +min/max(T) = 628.016, 842.701 +GAMG: Solving for p, Initial residual = 0.0903228, Final residual = 0.00156997, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.47013e-06, global = 1.4399e-06, cumulative = 0.000236438 +GAMG: Solving for p, Initial residual = 0.00163124, Final residual = 2.64797e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.43051e-06, global = 1.4305e-06, cumulative = 0.000237869 +smoothSolver: Solving for epsilon, Initial residual = 0.00104107, Final residual = 1.79005e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00460393, Final residual = 7.64535e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094062 s +other Time = 0 s +rho Equations = 0.000168 s +U Equations = 0.001112 s +Y Equations = 0.00246482 s +E Equations = 0.000621 s +p Equations = 0.00203 s +calculate parcels = 11.4575 s +chemistry correctThermo = 0.002093 s +turbulence correct = 0.000922 s +combustion correct(in Y) = 0.0844582 s +percentage of chemistry = 89.7899 % +percentage of rho/U/Y/E = 4.64143 % +========Time details of each equation======= +rhoEqn Time = 0.00029 s +rhoEqn assamble = 0.000232 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001112 s +UEqn assamble = 0.000682 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00043 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001795 s +YEqn assamble = 0.000676 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000163 s +YEqn correct boundary = 0 s +EEqn Time = 0.000461 s +EEqn assamble = 0.000345 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 28.58 s ClockTime = 29 s +Courant Number mean: 0.000217177 max: 0.0182758 +Time = 0.0005 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 53 new parcels + +Cloud: sprayCloud + Current number of parcels = 7712 + Current mass in system = 7.94548e-10 + Linear momentum = (3.15067e-11 -7.71009e-09 0) + |Linear momentum| = 7.71016e-09 + Linear kinetic energy = 3.9653e-08 + model1: + number of parcels added = 7717 + mass introduced = 8.0493e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.168, 509.906 + Mass transfer phase change = 1.0382e-11 + D10, D32, Dmax (mu) = 44.5749, 78.3861, 149.151 + Liquid penetration 95% mass (m) = 0.00408757 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00446235, Final residual = 7.06831e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00767714, Final residual = 2.30149e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00317225, Final residual = 2.28708e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00338266, Final residual = 1.63266e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00358845, Final residual = 1.89336e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00358847, Final residual = 1.89509e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00273666, Final residual = 1.89418e-07, No Iterations 1 +min/max(T) = 627.767, 843.085 +GAMG: Solving for p, Initial residual = 0.101497, Final residual = 0.0019846, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.49069e-06, global = 1.45703e-06, cumulative = 0.000239326 +GAMG: Solving for p, Initial residual = 0.0020613, Final residual = 6.44189e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.44772e-06, global = 1.4477e-06, cumulative = 0.000240774 +smoothSolver: Solving for epsilon, Initial residual = 0.00104405, Final residual = 1.79469e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00458139, Final residual = 7.60645e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09263 s +other Time = 0 s +rho Equations = 0.000184 s +U Equations = 0.001127 s +Y Equations = 0.00253976 s +E Equations = 0.000602 s +p Equations = 0.002447 s +calculate parcels = 11.5966 s +chemistry correctThermo = 0.002748 s +turbulence correct = 0.000993 s +combustion correct(in Y) = 0.0818092 s +percentage of chemistry = 88.3183 % +percentage of rho/U/Y/E = 4.80704 % +========Time details of each equation======= +rhoEqn Time = 0.000334 s +rhoEqn assamble = 0.000263 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001127 s +UEqn assamble = 0.00069 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000437 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001893 s +YEqn assamble = 0.000704 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00018 s +YEqn correct boundary = 0 s +EEqn Time = 0.000445 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00011 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 28.95 s ClockTime = 29 s +Courant Number mean: 0.000219078 max: 0.0182965 +Time = 0.0005025 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 41 new parcels + +Cloud: sprayCloud + Current number of parcels = 7753 + Current mass in system = 7.97992e-10 + Linear momentum = (3.17759e-11 -7.73693e-09 0) + |Linear momentum| = 7.73699e-09 + Linear kinetic energy = 3.97627e-08 + model1: + number of parcels added = 7758 + mass introduced = 8.08501e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.158, 509.974 + Mass transfer phase change = 1.05089e-11 + D10, D32, Dmax (mu) = 44.6047, 78.3936, 149.157 + Liquid penetration 95% mass (m) = 0.00410645 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00460472, Final residual = 7.05455e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00691699, Final residual = 2.0802e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00315639, Final residual = 2.28731e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00336915, Final residual = 1.61493e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00357073, Final residual = 1.89021e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00357075, Final residual = 1.89194e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00271679, Final residual = 1.87354e-07, No Iterations 1 +min/max(T) = 627.543, 843.462 +GAMG: Solving for p, Initial residual = 0.109442, Final residual = 0.00172865, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.49423e-06, global = 1.46784e-06, cumulative = 0.000242242 +GAMG: Solving for p, Initial residual = 0.00177705, Final residual = 5.46348e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.46238e-06, global = 1.46237e-06, cumulative = 0.000243704 +smoothSolver: Solving for epsilon, Initial residual = 0.00104748, Final residual = 1.80008e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00456004, Final residual = 7.57004e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092441 s +other Time = 0 s +rho Equations = 0.000155 s +U Equations = 0.001047 s +Y Equations = 0.00236044 s +E Equations = 0.000606 s +p Equations = 0.002471 s +calculate parcels = 11.7181 s +chemistry correctThermo = 0.002773 s +turbulence correct = 0.001036 s +combustion correct(in Y) = 0.0818086 s +percentage of chemistry = 88.4981 % +percentage of rho/U/Y/E = 4.5093 % +========Time details of each equation======= +rhoEqn Time = 0.000302 s +rhoEqn assamble = 0.000238 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001047 s +UEqn assamble = 0.000657 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00039 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001765 s +YEqn assamble = 0.000676 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000198 s +YEqn correct boundary = 0 s +EEqn Time = 0.000447 s +EEqn assamble = 0.000334 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 29.17 s ClockTime = 30 s +Courant Number mean: 0.000220916 max: 0.0183096 +Time = 0.000505 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 7802 + Current mass in system = 8.0211e-10 + Linear momentum = (3.21286e-11 -7.77238e-09 0) + |Linear momentum| = 7.77245e-09 + Linear kinetic energy = 3.99295e-08 + model1: + number of parcels added = 7807 + mass introduced = 8.12747e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.165, 510.038 + Mass transfer phase change = 1.0637e-11 + D10, D32, Dmax (mu) = 44.6558, 78.4237, 149.163 + Liquid penetration 95% mass (m) = 0.00412593 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00463401, Final residual = 7.26267e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00621472, Final residual = 9.89986e-07, No Iterations 1 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00313628, Final residual = 2.29836e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00335575, Final residual = 1.61496e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00355313, Final residual = 1.88665e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00355315, Final residual = 1.88837e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0026979, Final residual = 1.8785e-07, No Iterations 1 +min/max(T) = 627.333, 843.843 +GAMG: Solving for p, Initial residual = 0.12223, Final residual = 0.00193399, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.50902e-06, global = 1.48448e-06, cumulative = 0.000245188 +GAMG: Solving for p, Initial residual = 0.00196982, Final residual = 3.93509e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.47673e-06, global = 1.47672e-06, cumulative = 0.000246665 +smoothSolver: Solving for epsilon, Initial residual = 0.00105075, Final residual = 1.80566e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00453822, Final residual = 7.53422e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094329 s +other Time = 0 s +rho Equations = 0.00016 s +U Equations = 0.001125 s +Y Equations = 0.00237614 s +E Equations = 0.000599 s +p Equations = 0.001993 s +calculate parcels = 11.8798 s +chemistry correctThermo = 0.00232 s +turbulence correct = 0.000833 s +combustion correct(in Y) = 0.0847299 s +percentage of chemistry = 89.8238 % +percentage of rho/U/Y/E = 4.51626 % +========Time details of each equation======= +rhoEqn Time = 0.000278 s +rhoEqn assamble = 0.000222 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001125 s +UEqn assamble = 0.000747 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000378 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001728 s +YEqn assamble = 0.00066 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00017 s +YEqn correct boundary = 0 s +EEqn Time = 0.000445 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 29.42 s ClockTime = 30 s +Courant Number mean: 0.000222739 max: 0.0183551 +Time = 0.0005075 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 38 new parcels + +Cloud: sprayCloud + Current number of parcels = 7840 + Current mass in system = 8.05268e-10 + Linear momentum = (3.31149e-11 -7.79531e-09 0) + |Linear momentum| = 7.79538e-09 + Linear kinetic energy = 4.00128e-08 + model1: + number of parcels added = 7845 + mass introduced = 8.16034e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.145, 510.098 + Mass transfer phase change = 1.07662e-11 + D10, D32, Dmax (mu) = 44.6978, 78.4296, 149.168 + Liquid penetration 95% mass (m) = 0.00414516 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00497811, Final residual = 8.11706e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00555349, Final residual = 8.91969e-07, No Iterations 1 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00311605, Final residual = 2.29774e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00334115, Final residual = 1.61214e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00353685, Final residual = 1.88181e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00353686, Final residual = 1.88353e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00267231, Final residual = 1.86839e-07, No Iterations 1 +min/max(T) = 627.127, 844.224 +GAMG: Solving for p, Initial residual = 0.133537, Final residual = 0.00185197, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.52025e-06, global = 1.49793e-06, cumulative = 0.000248163 +GAMG: Solving for p, Initial residual = 0.00183682, Final residual = 4.95037e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.4895e-06, global = 1.4895e-06, cumulative = 0.000249653 +smoothSolver: Solving for epsilon, Initial residual = 0.00105439, Final residual = 1.81202e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00451679, Final residual = 7.50029e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.106234 s +other Time = 0 s +rho Equations = 0.000175 s +U Equations = 0.001083 s +Y Equations = 0.00244284 s +E Equations = 0.000616 s +p Equations = 0.002547 s +calculate parcels = 12.0184 s +chemistry correctThermo = 0.002773 s +turbulence correct = 0.001016 s +combustion correct(in Y) = 0.0953712 s +percentage of chemistry = 89.7746 % +percentage of rho/U/Y/E = 4.06352 % +========Time details of each equation======= +rhoEqn Time = 0.000328 s +rhoEqn assamble = 0.000258 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001082 s +UEqn assamble = 0.000704 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000378 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001783 s +YEqn assamble = 0.000681 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000169 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 29.67 s ClockTime = 30 s +Courant Number mean: 0.000224469 max: 0.0184072 +Time = 0.00051 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 68 new parcels + +Cloud: sprayCloud + Current number of parcels = 7908 + Current mass in system = 8.10982e-10 + Linear momentum = (3.29389e-11 -7.85139e-09 0) + |Linear momentum| = 7.85146e-09 + Linear kinetic energy = 4.03136e-08 + model1: + number of parcels added = 7913 + mass introduced = 8.21878e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.153, 510.155 + Mass transfer phase change = 1.08967e-11 + D10, D32, Dmax (mu) = 44.6993, 78.4233, 149.174 + Liquid penetration 95% mass (m) = 0.00416322 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00512478, Final residual = 8.52879e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00496828, Final residual = 8.15356e-07, No Iterations 1 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00310597, Final residual = 2.34754e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00332832, Final residual = 1.61096e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00352071, Final residual = 1.87691e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00352073, Final residual = 1.87862e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00266294, Final residual = 1.8823e-07, No Iterations 1 +min/max(T) = 626.936, 844.607 +GAMG: Solving for p, Initial residual = 0.14356, Final residual = 0.00254048, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.54192e-06, global = 1.51299e-06, cumulative = 0.000251166 +GAMG: Solving for p, Initial residual = 0.00246173, Final residual = 8.87972e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.50408e-06, global = 1.50407e-06, cumulative = 0.00025267 +smoothSolver: Solving for epsilon, Initial residual = 0.00105718, Final residual = 1.81679e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00449491, Final residual = 7.46464e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.066629 s +other Time = 0 s +rho Equations = 0.000163 s +U Equations = 0.001083 s +Y Equations = 0.00219499 s +E Equations = 0.000525 s +p Equations = 0.00199 s +calculate parcels = 12.1584 s +chemistry correctThermo = 0.001949 s +turbulence correct = 0.000885 s +combustion correct(in Y) = 0.057661 s +percentage of chemistry = 86.5404 % +percentage of rho/U/Y/E = 5.95235 % +========Time details of each equation======= +rhoEqn Time = 0.000299 s +rhoEqn assamble = 0.000227 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001082 s +UEqn assamble = 0.000682 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.0004 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001598 s +YEqn assamble = 0.000589 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000148 s +YEqn correct boundary = 0 s +EEqn Time = 0.00039 s +EEqn assamble = 0.000295 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 29.88 s ClockTime = 30 s +Courant Number mean: 0.00022619 max: 0.0184498 +Time = 0.0005125 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 59 new parcels + +Cloud: sprayCloud + Current number of parcels = 7967 + Current mass in system = 8.15953e-10 + Linear momentum = (3.18847e-11 -7.89764e-09 0) + |Linear momentum| = 7.89771e-09 + Linear kinetic energy = 4.05492e-08 + model1: + number of parcels added = 7972 + mass introduced = 8.26982e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.145, 511.71 + Mass transfer phase change = 1.10282e-11 + D10, D32, Dmax (mu) = 44.7648, 78.4789, 149.18 + Liquid penetration 95% mass (m) = 0.00418223 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00542263, Final residual = 8.57448e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00428331, Final residual = 7.17928e-07, No Iterations 1 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00307539, Final residual = 2.31255e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0033118, Final residual = 1.62848e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00350309, Final residual = 1.8713e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00350311, Final residual = 1.87299e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00264616, Final residual = 1.89778e-07, No Iterations 1 +min/max(T) = 626.78, 844.984 +GAMG: Solving for p, Initial residual = 0.139446, Final residual = 0.00198758, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.54573e-06, global = 1.52151e-06, cumulative = 0.000254191 +GAMG: Solving for p, Initial residual = 0.00191181, Final residual = 3.59466e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.51584e-06, global = 1.51584e-06, cumulative = 0.000255707 +smoothSolver: Solving for epsilon, Initial residual = 0.00106064, Final residual = 1.82232e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00447479, Final residual = 7.43207e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.067678 s +other Time = 0 s +rho Equations = 0.000148 s +U Equations = 0.000947 s +Y Equations = 0.00208185 s +E Equations = 0.0005 s +p Equations = 0.002151 s +calculate parcels = 12.2669 s +chemistry correctThermo = 0.001934 s +turbulence correct = 0.000892 s +combustion correct(in Y) = 0.0588531 s +percentage of chemistry = 86.9605 % +percentage of rho/U/Y/E = 5.43286 % +========Time details of each equation======= +rhoEqn Time = 0.000278 s +rhoEqn assamble = 0.00022 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000946 s +UEqn assamble = 0.000611 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000335 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001503 s +YEqn assamble = 0.000565 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000117 s +YEqn correct boundary = 0 s +EEqn Time = 0.00038 s +EEqn assamble = 0.000279 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000101 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 30.05 s ClockTime = 30 s +Courant Number mean: 0.000227766 max: 0.0184956 +Time = 0.000515 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 61 new parcels + +Cloud: sprayCloud + Current number of parcels = 8028 + Current mass in system = 8.2111e-10 + Linear momentum = (3.1652e-11 -7.946e-09 0) + |Linear momentum| = 7.94606e-09 + Linear kinetic energy = 4.07979e-08 + model1: + number of parcels added = 8033 + mass introduced = 8.32271e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.145, 515.557 + Mass transfer phase change = 1.11609e-11 + D10, D32, Dmax (mu) = 44.3427, 78.4664, 149.185 + Liquid penetration 95% mass (m) = 0.00420116 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00521405, Final residual = 8.18349e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00401796, Final residual = 6.8773e-07, No Iterations 1 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00305891, Final residual = 2.30029e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00329852, Final residual = 1.64179e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00348784, Final residual = 1.8657e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00348786, Final residual = 1.86739e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00263933, Final residual = 1.92127e-07, No Iterations 1 +min/max(T) = 626.645, 845.364 +GAMG: Solving for p, Initial residual = 0.124186, Final residual = 0.00198822, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.56296e-06, global = 1.53844e-06, cumulative = 0.000257245 +GAMG: Solving for p, Initial residual = 0.00184098, Final residual = 5.52034e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.52906e-06, global = 1.52905e-06, cumulative = 0.000258774 +smoothSolver: Solving for epsilon, Initial residual = 0.00106347, Final residual = 1.8268e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0044546, Final residual = 7.399e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.099607 s +other Time = 0 s +rho Equations = 0.000185 s +U Equations = 0.001333 s +Y Equations = 0.00246135 s +E Equations = 0.000638 s +p Equations = 0.002349 s +calculate parcels = 12.3737 s +chemistry correctThermo = 0.002781 s +turbulence correct = 0.00096 s +combustion correct(in Y) = 0.0887027 s +percentage of chemistry = 89.0526 % +percentage of rho/U/Y/E = 4.63557 % +========Time details of each equation======= +rhoEqn Time = 0.000321 s +rhoEqn assamble = 0.00025 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001331 s +UEqn assamble = 0.000838 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000493 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001697 s +YEqn assamble = 0.000648 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000136 s +YEqn correct boundary = 0 s +EEqn Time = 0.00048 s +EEqn assamble = 0.000361 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000119 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 30.26 s ClockTime = 31 s +Courant Number mean: 0.000229277 max: 0.0185375 +Time = 0.0005175 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 42 new parcels + +Cloud: sprayCloud + Current number of parcels = 8070 + Current mass in system = 8.24631e-10 + Linear momentum = (3.12098e-11 -7.97309e-09 0) + |Linear momentum| = 7.97315e-09 + Linear kinetic energy = 4.09059e-08 + model1: + number of parcels added = 8075 + mass introduced = 8.35925e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.144, 518.752 + Mass transfer phase change = 1.12944e-11 + D10, D32, Dmax (mu) = 44.3322, 78.4564, 149.191 + Liquid penetration 95% mass (m) = 0.00421933 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00534686, Final residual = 8.03743e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00407901, Final residual = 6.94707e-07, No Iterations 1 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0030553, Final residual = 2.33469e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00328096, Final residual = 1.62278e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00347125, Final residual = 1.86049e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00347127, Final residual = 1.86217e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00261749, Final residual = 1.89021e-07, No Iterations 1 +min/max(T) = 626.512, 845.741 +GAMG: Solving for p, Initial residual = 0.111122, Final residual = 0.00216831, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.58101e-06, global = 1.5449e-06, cumulative = 0.000260319 +GAMG: Solving for p, Initial residual = 0.00202237, Final residual = 6.32969e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.53894e-06, global = 1.53893e-06, cumulative = 0.000261858 +smoothSolver: Solving for epsilon, Initial residual = 0.00106713, Final residual = 1.83287e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00443527, Final residual = 7.36909e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.087798 s +other Time = 0 s +rho Equations = 0.00017 s +U Equations = 0.001057 s +Y Equations = 0.00202838 s +E Equations = 0.000662 s +p Equations = 0.004023 s +calculate parcels = 12.5187 s +chemistry correctThermo = 0.005197 s +turbulence correct = 0.001692 s +combustion correct(in Y) = 0.0727536 s +percentage of chemistry = 82.8648 % +percentage of rho/U/Y/E = 4.46181 % +========Time details of each equation======= +rhoEqn Time = 0.000483 s +rhoEqn assamble = 0.000346 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000137 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001057 s +UEqn assamble = 0.000691 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000366 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001383 s +YEqn assamble = 0.000533 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.1e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.00054 s +EEqn assamble = 0.000304 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000236 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 30.49 s ClockTime = 31 s +Courant Number mean: 0.000230587 max: 0.0185659 +Time = 0.00052 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 8121 + Current mass in system = 8.28913e-10 + Linear momentum = (3.04913e-11 -8.00995e-09 0) + |Linear momentum| = 8.01001e-09 + Linear kinetic energy = 4.10776e-08 + model1: + number of parcels added = 8126 + mass introduced = 8.40342e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.165, 521.347 + Mass transfer phase change = 1.14287e-11 + D10, D32, Dmax (mu) = 44.3012, 78.4694, 149.197 + Liquid penetration 95% mass (m) = 0.00423815 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00524746, Final residual = 7.97418e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0045449, Final residual = 7.7622e-07, No Iterations 1 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00302143, Final residual = 2.27496e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00326413, Final residual = 1.61034e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00345649, Final residual = 1.85379e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00345651, Final residual = 1.85545e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00259426, Final residual = 1.87433e-07, No Iterations 1 +min/max(T) = 626.38, 846.121 +GAMG: Solving for p, Initial residual = 0.0964084, Final residual = 0.00172966, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.58695e-06, global = 1.55572e-06, cumulative = 0.000263414 +GAMG: Solving for p, Initial residual = 0.00161138, Final residual = 4.02821e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.54828e-06, global = 1.54827e-06, cumulative = 0.000264962 +smoothSolver: Solving for epsilon, Initial residual = 0.00107088, Final residual = 1.83956e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00441552, Final residual = 7.34056e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.073809 s +other Time = 0 s +rho Equations = 0.000172 s +U Equations = 0.001118 s +Y Equations = 0.00202335 s +E Equations = 0.000493 s +p Equations = 0.001945 s +calculate parcels = 12.6705 s +chemistry correctThermo = 0.002013 s +turbulence correct = 0.000817 s +combustion correct(in Y) = 0.0650346 s +percentage of chemistry = 88.1121 % +percentage of rho/U/Y/E = 5.15703 % +========Time details of each equation======= +rhoEqn Time = 0.000288 s +rhoEqn assamble = 0.000226 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001117 s +UEqn assamble = 0.000732 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000385 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001382 s +YEqn assamble = 0.000523 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.5e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000374 s +EEqn assamble = 0.000278 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 30.72 s ClockTime = 31 s +Courant Number mean: 0.000231738 max: 0.0185877 +Time = 0.0005225 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 8170 + Current mass in system = 8.33017e-10 + Linear momentum = (2.87509e-11 -8.04448e-09 0) + |Linear momentum| = 8.04453e-09 + Linear kinetic energy = 4.12333e-08 + model1: + number of parcels added = 8175 + mass introduced = 8.44581e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.148, 523.388 + Mass transfer phase change = 1.15638e-11 + D10, D32, Dmax (mu) = 44.3439, 78.5029, 149.202 + Liquid penetration 95% mass (m) = 0.00425735 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00514973, Final residual = 8.27193e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00542194, Final residual = 8.99936e-07, No Iterations 1 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00298746, Final residual = 2.27299e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00324639, Final residual = 1.60835e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0034414, Final residual = 1.84717e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00344142, Final residual = 1.84881e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0025687, Final residual = 1.86285e-07, No Iterations 1 +min/max(T) = 626.249, 846.503 +GAMG: Solving for p, Initial residual = 0.0849215, Final residual = 0.00132638, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.59253e-06, global = 1.56337e-06, cumulative = 0.000266526 +GAMG: Solving for p, Initial residual = 0.00125202, Final residual = 2.77706e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.55699e-06, global = 1.55698e-06, cumulative = 0.000268083 +smoothSolver: Solving for epsilon, Initial residual = 0.00107469, Final residual = 1.84681e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00439598, Final residual = 7.31354e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.086746 s +other Time = 0 s +rho Equations = 0.000142 s +U Equations = 0.000884 s +Y Equations = 0.00234181 s +E Equations = 0.000641 s +p Equations = 0.002381 s +calculate parcels = 12.7866 s +chemistry correctThermo = 0.002746 s +turbulence correct = 0.000966 s +combustion correct(in Y) = 0.0764422 s +percentage of chemistry = 88.1219 % +percentage of rho/U/Y/E = 4.62132 % +========Time details of each equation======= +rhoEqn Time = 0.000288 s +rhoEqn assamble = 0.000227 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000883 s +UEqn assamble = 0.000579 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000304 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001719 s +YEqn assamble = 0.000638 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000175 s +YEqn correct boundary = 0 s +EEqn Time = 0.000482 s +EEqn assamble = 0.000364 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 30.92 s ClockTime = 31 s +Courant Number mean: 0.000232776 max: 0.0186297 +Time = 0.000525 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 66 new parcels + +Cloud: sprayCloud + Current number of parcels = 8235 + Current mass in system = 8.3858e-10 + Linear momentum = (2.77609e-11 -8.09762e-09 0) + |Linear momentum| = 8.09767e-09 + Linear kinetic energy = 4.15102e-08 + model1: + number of parcels added = 8241 + mass introduced = 8.50281e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.173, 524.908 + Mass transfer phase change = 1.17007e-11 + D10, D32, Dmax (mu) = 44.9565, 78.5093, 149.208 + Liquid penetration 95% mass (m) = 0.00427608 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0049484, Final residual = 8.11256e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00630382, Final residual = 2.00167e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00297854, Final residual = 2.3235e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00323979, Final residual = 1.63631e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00342739, Final residual = 1.83991e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00342741, Final residual = 1.84152e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00256002, Final residual = 1.89626e-07, No Iterations 1 +min/max(T) = 626.162, 846.884 +GAMG: Solving for p, Initial residual = 0.077098, Final residual = 0.00139539, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.61422e-06, global = 1.58405e-06, cumulative = 0.000269667 +GAMG: Solving for p, Initial residual = 0.00130845, Final residual = 5.97022e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.57779e-06, global = 1.57777e-06, cumulative = 0.000271244 +smoothSolver: Solving for epsilon, Initial residual = 0.00107766, Final residual = 1.85218e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00437543, Final residual = 7.28149e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09536 s +other Time = 0 s +rho Equations = 0.000166 s +U Equations = 0.001183 s +Y Equations = 0.00241217 s +E Equations = 0.000598 s +p Equations = 0.00238 s +calculate parcels = 12.9249 s +chemistry correctThermo = 0.002821 s +turbulence correct = 0.001339 s +combustion correct(in Y) = 0.0842638 s +percentage of chemistry = 88.3639 % +percentage of rho/U/Y/E = 4.57127 % +========Time details of each equation======= +rhoEqn Time = 0.000306 s +rhoEqn assamble = 0.000242 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001183 s +UEqn assamble = 0.000734 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000449 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001729 s +YEqn assamble = 0.000658 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000156 s +YEqn correct boundary = 0 s +EEqn Time = 0.000446 s +EEqn assamble = 0.000333 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 31.15 s ClockTime = 32 s +Courant Number mean: 0.000233753 max: 0.0186915 +Time = 0.0005275 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 64 new parcels + +Cloud: sprayCloud + Current number of parcels = 8298 + Current mass in system = 8.44001e-10 + Linear momentum = (2.8506e-11 -8.14887e-09 0) + |Linear momentum| = 8.14892e-09 + Linear kinetic energy = 4.17735e-08 + model1: + number of parcels added = 8305 + mass introduced = 8.55839e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.158, 525.944 + Mass transfer phase change = 1.18381e-11 + D10, D32, Dmax (mu) = 46.1619, 78.5615, 149.214 + Liquid penetration 95% mass (m) = 0.00429453 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0048263, Final residual = 7.66845e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00702088, Final residual = 2.10915e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00294656, Final residual = 2.33799e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00321974, Final residual = 1.64188e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0034128, Final residual = 1.83745e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00341282, Final residual = 1.83905e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00253903, Final residual = 1.89697e-07, No Iterations 1 +min/max(T) = 626.101, 847.262 +GAMG: Solving for p, Initial residual = 0.0655223, Final residual = 0.00102951, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.61406e-06, global = 1.58926e-06, cumulative = 0.000272834 +GAMG: Solving for p, Initial residual = 0.000948682, Final residual = 2.65535e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.58322e-06, global = 1.58321e-06, cumulative = 0.000274417 +smoothSolver: Solving for epsilon, Initial residual = 0.00108092, Final residual = 1.8586e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00435661, Final residual = 7.25519e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.089593 s +other Time = 1e-06 s +rho Equations = 0.000178 s +U Equations = 0.001135 s +Y Equations = 0.00233896 s +E Equations = 0.000629 s +p Equations = 0.002358 s +calculate parcels = 13.0741 s +chemistry correctThermo = 0.002578 s +turbulence correct = 0.000974 s +combustion correct(in Y) = 0.079209 s +percentage of chemistry = 88.4099 % +percentage of rho/U/Y/E = 4.77823 % +========Time details of each equation======= +rhoEqn Time = 0.000331 s +rhoEqn assamble = 0.000262 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001133 s +UEqn assamble = 0.000686 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000447 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001694 s +YEqn assamble = 0.000643 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00017 s +YEqn correct boundary = 0 s +EEqn Time = 0.000475 s +EEqn assamble = 0.000359 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 31.39 s ClockTime = 32 s +Courant Number mean: 0.000234629 max: 0.018727 +Time = 0.00053 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 47 new parcels + +Cloud: sprayCloud + Current number of parcels = 8345 + Current mass in system = 8.47965e-10 + Linear momentum = (2.77522e-11 -8.1812e-09 0) + |Linear momentum| = 8.18124e-09 + Linear kinetic energy = 4.1913e-08 + model1: + number of parcels added = 8352 + mass introduced = 8.5994e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.142, 526.538 + Mass transfer phase change = 1.19749e-11 + D10, D32, Dmax (mu) = 46.0305, 78.5767, 149.22 + Liquid penetration 95% mass (m) = 0.00431356 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00456145, Final residual = 7.13108e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00773947, Final residual = 2.2827e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00289274, Final residual = 2.25637e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00319218, Final residual = 1.61453e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00339972, Final residual = 1.83505e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00339974, Final residual = 1.83664e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00250666, Final residual = 1.85449e-07, No Iterations 1 +min/max(T) = 626.027, 847.64 +GAMG: Solving for p, Initial residual = 0.0578535, Final residual = 0.00123601, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.61902e-06, global = 1.58406e-06, cumulative = 0.000276001 +GAMG: Solving for p, Initial residual = 0.00117014, Final residual = 3.90071e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.57733e-06, global = 1.57732e-06, cumulative = 0.000277578 +smoothSolver: Solving for epsilon, Initial residual = 0.00108525, Final residual = 1.86763e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00433972, Final residual = 7.23628e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.087172 s +other Time = 0 s +rho Equations = 0.000181 s +U Equations = 0.00099 s +Y Equations = 0.00239832 s +E Equations = 0.000609 s +p Equations = 0.00241 s +calculate parcels = 13.201 s +chemistry correctThermo = 0.002758 s +turbulence correct = 0.000928 s +combustion correct(in Y) = 0.0767257 s +percentage of chemistry = 88.0164 % +percentage of rho/U/Y/E = 4.79319 % +========Time details of each equation======= +rhoEqn Time = 0.000326 s +rhoEqn assamble = 0.00026 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000989 s +UEqn assamble = 0.000602 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000387 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001811 s +YEqn assamble = 0.000674 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000219 s +YEqn correct boundary = 0 s +EEqn Time = 0.000453 s +EEqn assamble = 0.000339 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 31.61 s ClockTime = 32 s +Courant Number mean: 0.000235388 max: 0.0187737 +Time = 0.0005325 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 52 new parcels + +Cloud: sprayCloud + Current number of parcels = 8397 + Current mass in system = 8.52353e-10 + Linear momentum = (2.68039e-11 -8.21885e-09 0) + |Linear momentum| = 8.21889e-09 + Linear kinetic energy = 4.2087e-08 + model1: + number of parcels added = 8404 + mass introduced = 8.64465e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.154, 526.707 + Mass transfer phase change = 1.21124e-11 + D10, D32, Dmax (mu) = 46.043, 78.5972, 149.225 + Liquid penetration 95% mass (m) = 0.00433198 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00422375, Final residual = 6.68476e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0085789, Final residual = 2.5419e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0028705, Final residual = 2.23303e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00317571, Final residual = 1.60015e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00338657, Final residual = 1.83227e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00338659, Final residual = 1.83386e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0024827, Final residual = 1.8295e-07, No Iterations 1 +min/max(T) = 625.941, 848.023 +GAMG: Solving for p, Initial residual = 0.0512984, Final residual = 0.000823293, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.61627e-06, global = 1.58911e-06, cumulative = 0.000279167 +GAMG: Solving for p, Initial residual = 0.000781133, Final residual = 1.64647e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.58393e-06, global = 1.58393e-06, cumulative = 0.000280751 +smoothSolver: Solving for epsilon, Initial residual = 0.00108923, Final residual = 1.87642e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00432189, Final residual = 7.21565e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.074975 s +other Time = 0 s +rho Equations = 0.000143 s +U Equations = 0.000933 s +Y Equations = 0.00206131 s +E Equations = 0.000494 s +p Equations = 0.001992 s +calculate parcels = 13.3166 s +chemistry correctThermo = 0.001992 s +turbulence correct = 0.000812 s +combustion correct(in Y) = 0.0663817 s +percentage of chemistry = 88.5384 % +percentage of rho/U/Y/E = 4.84336 % +========Time details of each equation======= +rhoEqn Time = 0.00027 s +rhoEqn assamble = 0.000207 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000933 s +UEqn assamble = 0.000574 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000359 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001496 s +YEqn assamble = 0.000567 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000141 s +YEqn correct boundary = 0 s +EEqn Time = 0.000375 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 31.8 s ClockTime = 32 s +Courant Number mean: 0.000236164 max: 0.0188263 +Time = 0.000535 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 57 new parcels + +Cloud: sprayCloud + Current number of parcels = 8454 + Current mass in system = 8.57173e-10 + Linear momentum = (2.63147e-11 -8.26201e-09 0) + |Linear momentum| = 8.26205e-09 + Linear kinetic energy = 4.22965e-08 + model1: + number of parcels added = 8461 + mass introduced = 8.69424e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.149, 526.467 + Mass transfer phase change = 1.22503e-11 + D10, D32, Dmax (mu) = 46.0828, 78.6755, 149.341 + Liquid penetration 95% mass (m) = 0.00434919 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00409595, Final residual = 6.79293e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00936537, Final residual = 2.75574e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00284423, Final residual = 2.20171e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00315914, Final residual = 1.57798e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00337502, Final residual = 1.83044e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00337504, Final residual = 1.83202e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00245747, Final residual = 1.79836e-07, No Iterations 1 +min/max(T) = 625.876, 848.405 +GAMG: Solving for p, Initial residual = 0.0462094, Final residual = 0.000753109, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.62205e-06, global = 1.59353e-06, cumulative = 0.000282345 +GAMG: Solving for p, Initial residual = 0.000712555, Final residual = 7.7049e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.5896e-06, global = 1.58957e-06, cumulative = 0.000283934 +smoothSolver: Solving for epsilon, Initial residual = 0.00109327, Final residual = 1.88517e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00430415, Final residual = 7.195e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09506 s +other Time = 0 s +rho Equations = 0.00017 s +U Equations = 0.001201 s +Y Equations = 0.00242396 s +E Equations = 0.000609 s +p Equations = 0.002249 s +calculate parcels = 13.4509 s +chemistry correctThermo = 0.002792 s +turbulence correct = 0.001043 s +combustion correct(in Y) = 0.084373 s +percentage of chemistry = 88.7577 % +percentage of rho/U/Y/E = 4.63282 % +========Time details of each equation======= +rhoEqn Time = 0.00032 s +rhoEqn assamble = 0.000256 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.0012 s +UEqn assamble = 0.000754 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000446 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001775 s +YEqn assamble = 0.000653 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00019 s +YEqn correct boundary = 0 s +EEqn Time = 0.000456 s +EEqn assamble = 0.00034 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 32.03 s ClockTime = 32 s +Courant Number mean: 0.000236987 max: 0.0188669 +Time = 0.0005375 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 62 new parcels + +Cloud: sprayCloud + Current number of parcels = 8516 + Current mass in system = 8.62437e-10 + Linear momentum = (2.67261e-11 -8.31075e-09 0) + |Linear momentum| = 8.31079e-09 + Linear kinetic energy = 4.2541e-08 + model1: + number of parcels added = 8523 + mass introduced = 8.74826e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.142, 525.818 + Mass transfer phase change = 1.23888e-11 + D10, D32, Dmax (mu) = 46.0009, 78.6702, 149.237 + Liquid penetration 95% mass (m) = 0.00436637 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0039693, Final residual = 6.62932e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0101176, Final residual = 2.97883e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00282636, Final residual = 2.17528e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00314398, Final residual = 1.56611e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00336288, Final residual = 1.82745e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0033629, Final residual = 1.82902e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00244519, Final residual = 1.79539e-07, No Iterations 1 +min/max(T) = 625.82, 848.787 +GAMG: Solving for p, Initial residual = 0.0425331, Final residual = 0.00085344, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.63271e-06, global = 1.60067e-06, cumulative = 0.000285535 +GAMG: Solving for p, Initial residual = 0.000811522, Final residual = 3.00453e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.59674e-06, global = 1.59673e-06, cumulative = 0.000287132 +smoothSolver: Solving for epsilon, Initial residual = 0.00109636, Final residual = 1.89252e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00428553, Final residual = 7.17213e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.08152 s +other Time = 0 s +rho Equations = 0.000191 s +U Equations = 0.001177 s +Y Equations = 0.0022168 s +E Equations = 0.000512 s +p Equations = 0.002368 s +calculate parcels = 13.6039 s +chemistry correctThermo = 0.001972 s +turbulence correct = 0.001019 s +combustion correct(in Y) = 0.0718672 s +percentage of chemistry = 88.159 % +percentage of rho/U/Y/E = 5.02551 % +========Time details of each equation======= +rhoEqn Time = 0.000397 s +rhoEqn assamble = 0.000261 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000136 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001176 s +UEqn assamble = 0.000728 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000448 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001566 s +YEqn assamble = 0.000581 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000104 s +YEqn correct boundary = 0 s +EEqn Time = 0.000385 s +EEqn assamble = 0.000289 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 32.26 s ClockTime = 33 s +Courant Number mean: 0.000238003 max: 0.0189018 +Time = 0.00054 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 42 new parcels + +Cloud: sprayCloud + Current number of parcels = 8558 + Current mass in system = 8.65972e-10 + Linear momentum = (2.61172e-11 -8.33726e-09 0) + |Linear momentum| = 8.3373e-09 + Linear kinetic energy = 4.26411e-08 + model1: + number of parcels added = 8565 + mass introduced = 8.785e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.141, 524.775 + Mass transfer phase change = 1.25277e-11 + D10, D32, Dmax (mu) = 46.0155, 78.7024, 149.243 + Liquid penetration 95% mass (m) = 0.00438327 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00426137, Final residual = 6.98931e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0106937, Final residual = 3.07545e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00280851, Final residual = 2.14805e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0031277, Final residual = 1.55298e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0033518, Final residual = 1.82388e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00335182, Final residual = 1.82545e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00242407, Final residual = 1.77964e-07, No Iterations 1 +min/max(T) = 625.767, 849.166 +GAMG: Solving for p, Initial residual = 0.0383406, Final residual = 0.000700651, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.63473e-06, global = 1.60388e-06, cumulative = 0.000288736 +GAMG: Solving for p, Initial residual = 0.000679513, Final residual = 2.14574e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.6015e-06, global = 1.60149e-06, cumulative = 0.000290337 +smoothSolver: Solving for epsilon, Initial residual = 0.00110039, Final residual = 1.90151e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00426812, Final residual = 7.15212e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.073507 s +other Time = 0 s +rho Equations = 0.00016 s +U Equations = 0.000999 s +Y Equations = 0.00236524 s +E Equations = 0.000516 s +p Equations = 0.001997 s +calculate parcels = 13.7142 s +chemistry correctThermo = 0.001977 s +turbulence correct = 0.000847 s +combustion correct(in Y) = 0.0644668 s +percentage of chemistry = 87.7015 % +percentage of rho/U/Y/E = 5.4964 % +========Time details of each equation======= +rhoEqn Time = 0.000278 s +rhoEqn assamble = 0.000222 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000998 s +UEqn assamble = 0.000633 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000365 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001794 s +YEqn assamble = 0.000617 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000161 s +YEqn correct boundary = 0 s +EEqn Time = 0.000388 s +EEqn assamble = 0.000287 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000101 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 32.45 s ClockTime = 33 s +Courant Number mean: 0.000239024 max: 0.0189326 +Time = 0.0005425 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 8608 + Current mass in system = 8.70184e-10 + Linear momentum = (2.76768e-11 -8.37232e-09 0) + |Linear momentum| = 8.37236e-09 + Linear kinetic energy = 4.27964e-08 + model1: + number of parcels added = 8615 + mass introduced = 8.82852e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.139, 523.323 + Mass transfer phase change = 1.26673e-11 + D10, D32, Dmax (mu) = 45.9624, 78.7214, 149.249 + Liquid penetration 95% mass (m) = 0.00440243 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00429864, Final residual = 7.15744e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0114462, Final residual = 3.2923e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00279009, Final residual = 2.13198e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00311369, Final residual = 1.53944e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00334004, Final residual = 1.81951e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00334007, Final residual = 1.82107e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00241101, Final residual = 1.76391e-07, No Iterations 1 +min/max(T) = 625.716, 849.55 +GAMG: Solving for p, Initial residual = 0.0360596, Final residual = 0.000620057, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.63755e-06, global = 1.61034e-06, cumulative = 0.000291948 +GAMG: Solving for p, Initial residual = 0.000598618, Final residual = 6.56425e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.60864e-06, global = 1.6086e-06, cumulative = 0.000293556 +smoothSolver: Solving for epsilon, Initial residual = 0.0011039, Final residual = 1.91027e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00424983, Final residual = 7.13108e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.091023 s +other Time = 0 s +rho Equations = 0.000227 s +U Equations = 0.001112 s +Y Equations = 0.00233925 s +E Equations = 0.000623 s +p Equations = 0.002169 s +calculate parcels = 13.8228 s +chemistry correctThermo = 0.002787 s +turbulence correct = 0.000998 s +combustion correct(in Y) = 0.0804498 s +percentage of chemistry = 88.384 % +percentage of rho/U/Y/E = 4.72545 % +========Time details of each equation======= +rhoEqn Time = 0.000366 s +rhoEqn assamble = 0.000293 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001111 s +UEqn assamble = 0.00074 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000371 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001763 s +YEqn assamble = 0.000647 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000205 s +YEqn correct boundary = 0 s +EEqn Time = 0.000466 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000134 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 32.65 s ClockTime = 33 s +Courant Number mean: 0.000240098 max: 0.0189806 +Time = 0.000545 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 8654 + Current mass in system = 8.74032e-10 + Linear momentum = (2.64963e-11 -8.40249e-09 0) + |Linear momentum| = 8.40254e-09 + Linear kinetic energy = 4.29192e-08 + model1: + number of parcels added = 8661 + mass introduced = 8.86839e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.136, 521.477 + Mass transfer phase change = 1.28074e-11 + D10, D32, Dmax (mu) = 45.9743, 78.7454, 149.254 + Liquid penetration 95% mass (m) = 0.00441861 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00444379, Final residual = 7.37748e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0121521, Final residual = 3.4238e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00276606, Final residual = 2.12108e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00310003, Final residual = 1.53168e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00332966, Final residual = 1.81496e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00332968, Final residual = 1.81651e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00239571, Final residual = 1.75321e-07, No Iterations 1 +min/max(T) = 625.664, 849.932 +GAMG: Solving for p, Initial residual = 0.0328047, Final residual = 0.000486788, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.63893e-06, global = 1.61639e-06, cumulative = 0.000295173 +GAMG: Solving for p, Initial residual = 0.000471276, Final residual = 4.94839e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.61518e-06, global = 1.61516e-06, cumulative = 0.000296788 +smoothSolver: Solving for epsilon, Initial residual = 0.00110699, Final residual = 1.91832e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00423124, Final residual = 7.10959e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.083319 s +other Time = 0 s +rho Equations = 0.000184 s +U Equations = 0.001134 s +Y Equations = 0.00208764 s +E Equations = 0.000487 s +p Equations = 0.001851 s +calculate parcels = 13.9665 s +chemistry correctThermo = 0.001982 s +turbulence correct = 0.00083 s +combustion correct(in Y) = 0.0745604 s +percentage of chemistry = 89.4878 % +percentage of rho/U/Y/E = 4.67197 % +========Time details of each equation======= +rhoEqn Time = 0.000307 s +rhoEqn assamble = 0.000245 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001133 s +UEqn assamble = 0.000695 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000438 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001435 s +YEqn assamble = 0.000537 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000111 s +YEqn correct boundary = 0 s +EEqn Time = 0.000369 s +EEqn assamble = 0.000275 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 32.87 s ClockTime = 33 s +Courant Number mean: 0.000241191 max: 0.0190145 +Time = 0.0005475 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 40 new parcels + +Cloud: sprayCloud + Current number of parcels = 8694 + Current mass in system = 8.77336e-10 + Linear momentum = (2.67045e-11 -8.4256e-09 0) + |Linear momentum| = 8.42564e-09 + Linear kinetic energy = 4.29952e-08 + model1: + number of parcels added = 8701 + mass introduced = 8.90284e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.151, 519.278 + Mass transfer phase change = 1.29481e-11 + D10, D32, Dmax (mu) = 45.956, 78.7744, 149.26 + Liquid penetration 95% mass (m) = 0.00443736 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00453698, Final residual = 7.32092e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.01276, Final residual = 3.53921e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00272608, Final residual = 2.11205e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00308576, Final residual = 1.52671e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00331883, Final residual = 1.80981e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00331886, Final residual = 1.81135e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00237675, Final residual = 1.73251e-07, No Iterations 1 +min/max(T) = 625.628, 850.313 +GAMG: Solving for p, Initial residual = 0.031508, Final residual = 0.000624922, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.64821e-06, global = 1.62206e-06, cumulative = 0.00029841 +GAMG: Solving for p, Initial residual = 0.000610402, Final residual = 6.43275e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.62109e-06, global = 1.62105e-06, cumulative = 0.000300031 +smoothSolver: Solving for epsilon, Initial residual = 0.00111057, Final residual = 1.92735e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00421308, Final residual = 7.08856e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.08913 s +other Time = 0 s +rho Equations = 0.000158 s +U Equations = 0.0011 s +Y Equations = 0.0024491 s +E Equations = 0.000607 s +p Equations = 0.002163 s +calculate parcels = 14.1015 s +chemistry correctThermo = 0.002774 s +turbulence correct = 0.001014 s +combustion correct(in Y) = 0.0786709 s +percentage of chemistry = 88.2653 % +percentage of rho/U/Y/E = 4.84024 % +========Time details of each equation======= +rhoEqn Time = 0.000303 s +rhoEqn assamble = 0.000239 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001099 s +UEqn assamble = 0.000673 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000426 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00176 s +YEqn assamble = 0.000655 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000159 s +YEqn correct boundary = 0 s +EEqn Time = 0.000451 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 33.1 s ClockTime = 34 s +Courant Number mean: 0.000242269 max: 0.019088 +Time = 0.00055 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 42 new parcels + +Cloud: sprayCloud + Current number of parcels = 8736 + Current mass in system = 8.80779e-10 + Linear momentum = (2.59947e-11 -8.45021e-09 0) + |Linear momentum| = 8.45025e-09 + Linear kinetic energy = 4.30804e-08 + model1: + number of parcels added = 8743 + mass introduced = 8.93868e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.151, 516.754 + Mass transfer phase change = 1.30892e-11 + D10, D32, Dmax (mu) = 45.9647, 78.8186, 149.266 + Liquid penetration 95% mass (m) = 0.00445665 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00452284, Final residual = 7.41293e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0134344, Final residual = 3.68225e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00271792, Final residual = 2.08802e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00307184, Final residual = 1.50942e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00330798, Final residual = 1.80484e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00330801, Final residual = 1.80636e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00235742, Final residual = 1.70253e-07, No Iterations 1 +min/max(T) = 625.593, 850.698 +GAMG: Solving for p, Initial residual = 0.0289834, Final residual = 0.000539744, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.65615e-06, global = 1.62715e-06, cumulative = 0.000301658 +GAMG: Solving for p, Initial residual = 0.00052626, Final residual = 8.4638e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.62713e-06, global = 1.62708e-06, cumulative = 0.000303285 +smoothSolver: Solving for epsilon, Initial residual = 0.00111478, Final residual = 1.93756e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00419549, Final residual = 7.06961e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094768 s +other Time = 1e-06 s +rho Equations = 0.000171 s +U Equations = 0.001138 s +Y Equations = 0.00238379 s +E Equations = 0.000604 s +p Equations = 0.002234 s +calculate parcels = 14.2443 s +chemistry correctThermo = 0.002828 s +turbulence correct = 0.001006 s +combustion correct(in Y) = 0.0842042 s +percentage of chemistry = 88.853 % +percentage of rho/U/Y/E = 4.53401 % +========Time details of each equation======= +rhoEqn Time = 0.000313 s +rhoEqn assamble = 0.000248 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001137 s +UEqn assamble = 0.000693 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000444 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001745 s +YEqn assamble = 0.00065 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000177 s +YEqn correct boundary = 0 s +EEqn Time = 0.000444 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 33.33 s ClockTime = 34 s +Courant Number mean: 0.000243264 max: 0.0191634 +Time = 0.0005525 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 45 new parcels + +Cloud: sprayCloud + Current number of parcels = 8780 + Current mass in system = 8.84444e-10 + Linear momentum = (2.64542e-11 -8.47755e-09 0) + |Linear momentum| = 8.47759e-09 + Linear kinetic energy = 4.31815e-08 + model1: + number of parcels added = 8788 + mass introduced = 8.97676e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.141, 510.874 + Mass transfer phase change = 1.32317e-11 + D10, D32, Dmax (mu) = 52.5313, 78.8816, 149.272 + Liquid penetration 95% mass (m) = 0.00447453 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00438969, Final residual = 7.0646e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0140174, Final residual = 3.84621e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00270906, Final residual = 2.04826e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00306514, Final residual = 1.4852e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00329733, Final residual = 1.80001e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00329735, Final residual = 1.80151e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00234736, Final residual = 1.64683e-07, No Iterations 1 +min/max(T) = 625.533, 851.085 +GAMG: Solving for p, Initial residual = 0.0300038, Final residual = 0.000788005, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.68275e-06, global = 1.64075e-06, cumulative = 0.000304926 +GAMG: Solving for p, Initial residual = 0.000771576, Final residual = 9.29375e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.64202e-06, global = 1.64196e-06, cumulative = 0.000306568 +smoothSolver: Solving for epsilon, Initial residual = 0.001119, Final residual = 1.94804e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00417799, Final residual = 7.05163e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.089877 s +other Time = 1e-06 s +rho Equations = 0.000226 s +U Equations = 0.001666 s +Y Equations = 0.0024457 s +E Equations = 0.0005 s +p Equations = 0.001894 s +calculate parcels = 14.3992 s +chemistry correctThermo = 0.002005 s +turbulence correct = 0.000897 s +combustion correct(in Y) = 0.0800103 s +percentage of chemistry = 89.022 % +percentage of rho/U/Y/E = 5.38258 % +========Time details of each equation======= +rhoEqn Time = 0.000352 s +rhoEqn assamble = 0.00027 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001664 s +UEqn assamble = 0.000941 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000723 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001348 s +YEqn assamble = 0.000627 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -0.000112 s +YEqn correct boundary = 0 s +EEqn Time = 0.000378 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 33.58 s ClockTime = 34 s +Courant Number mean: 0.000244085 max: 0.0192103 +Time = 0.000555 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 53 new parcels + +Cloud: sprayCloud + Current number of parcels = 8833 + Current mass in system = 8.88756e-10 + Linear momentum = (2.61692e-11 -8.51261e-09 0) + |Linear momentum| = 8.51265e-09 + Linear kinetic energy = 4.33309e-08 + model1: + number of parcels added = 8841 + mass introduced = 9.0213e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.16, 510.923 + Mass transfer phase change = 1.33735e-11 + D10, D32, Dmax (mu) = 52.5413, 78.898, 149.278 + Liquid penetration 95% mass (m) = 0.00449258 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00406632, Final residual = 6.38899e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0144306, Final residual = 3.99373e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00275932, Final residual = 2.04493e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00304332, Final residual = 1.44726e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00328838, Final residual = 1.79537e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0032884, Final residual = 1.79686e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00233401, Final residual = 1.57975e-07, No Iterations 1 +min/max(T) = 625.436, 851.472 +GAMG: Solving for p, Initial residual = 0.028372, Final residual = 0.000603784, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.66787e-06, global = 1.63384e-06, cumulative = 0.000308202 +GAMG: Solving for p, Initial residual = 0.00058799, Final residual = 7.76344e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.63482e-06, global = 1.63477e-06, cumulative = 0.000309836 +smoothSolver: Solving for epsilon, Initial residual = 0.00112267, Final residual = 1.95784e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00416016, Final residual = 7.0327e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.090226 s +other Time = 0 s +rho Equations = 0.000183 s +U Equations = 0.001156 s +Y Equations = 0.00242244 s +E Equations = 0.000601 s +p Equations = 0.002186 s +calculate parcels = 14.5446 s +chemistry correctThermo = 0.002786 s +turbulence correct = 0.00095 s +combustion correct(in Y) = 0.0797386 s +percentage of chemistry = 88.3765 % +percentage of rho/U/Y/E = 4.83502 % +========Time details of each equation======= +rhoEqn Time = 0.000326 s +rhoEqn assamble = 0.00026 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001155 s +UEqn assamble = 0.000715 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00044 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001762 s +YEqn assamble = 0.000661 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000193 s +YEqn correct boundary = 0 s +EEqn Time = 0.000446 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 33.82 s ClockTime = 34 s +Courant Number mean: 0.000244808 max: 0.0192357 +Time = 0.0005575 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 42 new parcels + +Cloud: sprayCloud + Current number of parcels = 8875 + Current mass in system = 8.9213e-10 + Linear momentum = (2.74168e-11 -8.53583e-09 0) + |Linear momentum| = 8.53587e-09 + Linear kinetic energy = 4.34038e-08 + model1: + number of parcels added = 8883 + mass introduced = 9.05646e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.137, 510.974 + Mass transfer phase change = 1.35162e-11 + D10, D32, Dmax (mu) = 52.5581, 78.8995, 149.284 + Liquid penetration 95% mass (m) = 0.00451108 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00362203, Final residual = 5.76324e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0146293, Final residual = 4.07778e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00275048, Final residual = 2.03677e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00303372, Final residual = 1.44794e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00327772, Final residual = 1.78985e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00327774, Final residual = 1.79134e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00232928, Final residual = 1.56184e-07, No Iterations 1 +min/max(T) = 625.342, 851.859 +GAMG: Solving for p, Initial residual = 0.0283475, Final residual = 0.00045507, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.66779e-06, global = 1.64423e-06, cumulative = 0.000311481 +GAMG: Solving for p, Initial residual = 0.000441809, Final residual = 6.95461e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.64468e-06, global = 1.64465e-06, cumulative = 0.000313125 +smoothSolver: Solving for epsilon, Initial residual = 0.00112602, Final residual = 1.96708e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0041418, Final residual = 7.01146e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092326 s +other Time = 0 s +rho Equations = 0.000173 s +U Equations = 0.001109 s +Y Equations = 0.00235211 s +E Equations = 0.000635 s +p Equations = 0.002256 s +calculate parcels = 14.6861 s +chemistry correctThermo = 0.002786 s +turbulence correct = 0.000972 s +combustion correct(in Y) = 0.0818509 s +percentage of chemistry = 88.6542 % +percentage of rho/U/Y/E = 4.62395 % +========Time details of each equation======= +rhoEqn Time = 0.000321 s +rhoEqn assamble = 0.000255 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001108 s +UEqn assamble = 0.000674 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000434 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00166 s +YEqn assamble = 0.000628 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000144 s +YEqn correct boundary = 0 s +EEqn Time = 0.000461 s +EEqn assamble = 0.000344 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 34.05 s ClockTime = 34 s +Courant Number mean: 0.000245519 max: 0.0192777 +Time = 0.00056 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 56 new parcels + +Cloud: sprayCloud + Current number of parcels = 8931 + Current mass in system = 8.96636e-10 + Linear momentum = (2.82554e-11 -8.57287e-09 0) + |Linear momentum| = 8.57292e-09 + Linear kinetic energy = 4.35626e-08 + model1: + number of parcels added = 8939 + mass introduced = 9.10296e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.15, 511.027 + Mass transfer phase change = 1.36598e-11 + D10, D32, Dmax (mu) = 52.6169, 78.942, 149.29 + Liquid penetration 95% mass (m) = 0.00452922 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00348474, Final residual = 5.53104e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0147765, Final residual = 4.08632e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00272718, Final residual = 2.01887e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00302481, Final residual = 1.43831e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00326802, Final residual = 1.78425e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00326804, Final residual = 1.78572e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00232316, Final residual = 1.53811e-07, No Iterations 1 +min/max(T) = 625.249, 852.248 +GAMG: Solving for p, Initial residual = 0.0293438, Final residual = 0.000505921, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.68246e-06, global = 1.65372e-06, cumulative = 0.000314779 +GAMG: Solving for p, Initial residual = 0.00048852, Final residual = 7.27679e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.65478e-06, global = 1.65474e-06, cumulative = 0.000316434 +smoothSolver: Solving for epsilon, Initial residual = 0.00112896, Final residual = 1.97531e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00412288, Final residual = 6.98834e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.086334 s +other Time = 0 s +rho Equations = 0.000167 s +U Equations = 0.001102 s +Y Equations = 0.00207514 s +E Equations = 0.000523 s +p Equations = 0.001939 s +calculate parcels = 14.8116 s +chemistry correctThermo = 0.001964 s +turbulence correct = 0.000818 s +combustion correct(in Y) = 0.0775459 s +percentage of chemistry = 89.8208 % +percentage of rho/U/Y/E = 4.47928 % +========Time details of each equation======= +rhoEqn Time = 0.000287 s +rhoEqn assamble = 0.000227 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.0011 s +UEqn assamble = 0.000675 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000425 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001437 s +YEqn assamble = 0.000523 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000136 s +YEqn correct boundary = 0 s +EEqn Time = 0.000403 s +EEqn assamble = 0.000307 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 34.26 s ClockTime = 35 s +Courant Number mean: 0.000246298 max: 0.0193062 +Time = 0.0005625 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 8977 + Current mass in system = 9.00302e-10 + Linear momentum = (2.81074e-11 -8.5994e-09 0) + |Linear momentum| = 8.59944e-09 + Linear kinetic energy = 4.36541e-08 + model1: + number of parcels added = 8985 + mass introduced = 9.14107e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.147, 511.083 + Mass transfer phase change = 1.38042e-11 + D10, D32, Dmax (mu) = 52.6683, 78.9833, 149.296 + Liquid penetration 95% mass (m) = 0.00454738 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00357443, Final residual = 5.61754e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0149161, Final residual = 4.05122e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00270928, Final residual = 2.04394e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00301525, Final residual = 1.43127e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00325812, Final residual = 1.77771e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00325814, Final residual = 1.77918e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00232705, Final residual = 1.53256e-07, No Iterations 1 +min/max(T) = 625.182, 852.636 +GAMG: Solving for p, Initial residual = 0.0312853, Final residual = 0.000532019, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.69135e-06, global = 1.66319e-06, cumulative = 0.000318097 +GAMG: Solving for p, Initial residual = 0.00051822, Final residual = 6.53433e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.66435e-06, global = 1.66431e-06, cumulative = 0.000319761 +smoothSolver: Solving for epsilon, Initial residual = 0.00113241, Final residual = 1.984e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00410477, Final residual = 6.96612e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092313 s +other Time = 1e-06 s +rho Equations = 0.000169 s +U Equations = 0.001081 s +Y Equations = 0.00236448 s +E Equations = 0.000607 s +p Equations = 0.001847 s +calculate parcels = 14.967 s +chemistry correctThermo = 0.002757 s +turbulence correct = 0.000835 s +combustion correct(in Y) = 0.0824635 s +percentage of chemistry = 89.3303 % +percentage of rho/U/Y/E = 4.573 % +========Time details of each equation======= +rhoEqn Time = 0.000293 s +rhoEqn assamble = 0.000232 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001081 s +UEqn assamble = 0.000653 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000428 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001717 s +YEqn assamble = 0.000634 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000174 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000338 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 34.51 s ClockTime = 35 s +Courant Number mean: 0.000247134 max: 0.0193446 +Time = 0.000565 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 56 new parcels + +Cloud: sprayCloud + Current number of parcels = 9033 + Current mass in system = 9.04765e-10 + Linear momentum = (2.85736e-11 -8.63534e-09 0) + |Linear momentum| = 8.63539e-09 + Linear kinetic energy = 4.3803e-08 + model1: + number of parcels added = 9041 + mass introduced = 9.18715e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.141, 511.142 + Mass transfer phase change = 1.39496e-11 + D10, D32, Dmax (mu) = 50.4693, 78.9823, 149.301 + Liquid penetration 95% mass (m) = 0.00456348 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00355869, Final residual = 5.3679e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0149609, Final residual = 4.07711e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00270529, Final residual = 2.06499e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00300685, Final residual = 1.42556e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00324821, Final residual = 1.76979e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00324823, Final residual = 1.77124e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0023359, Final residual = 1.52379e-07, No Iterations 1 +min/max(T) = 625.108, 853.027 +GAMG: Solving for p, Initial residual = 0.0325501, Final residual = 0.000534428, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.70071e-06, global = 1.67564e-06, cumulative = 0.000321437 +GAMG: Solving for p, Initial residual = 0.00052755, Final residual = 8.2047e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.67568e-06, global = 1.67563e-06, cumulative = 0.000323112 +smoothSolver: Solving for epsilon, Initial residual = 0.00113545, Final residual = 1.99229e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00408592, Final residual = 6.942e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.070965 s +other Time = 0 s +rho Equations = 0.00016 s +U Equations = 0.001052 s +Y Equations = 0.00224819 s +E Equations = 0.000494 s +p Equations = 0.001839 s +calculate parcels = 15.1196 s +chemistry correctThermo = 0.001969 s +turbulence correct = 0.000812 s +combustion correct(in Y) = 0.0622098 s +percentage of chemistry = 87.6627 % +percentage of rho/U/Y/E = 5.57203 % +========Time details of each equation======= +rhoEqn Time = 0.000283 s +rhoEqn assamble = 0.000229 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001052 s +UEqn assamble = 0.000665 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000387 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001622 s +YEqn assamble = 0.000588 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000102 s +YEqn correct boundary = 0 s +EEqn Time = 0.000368 s +EEqn assamble = 0.000279 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 8.9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 34.73 s ClockTime = 35 s +Courant Number mean: 0.000248176 max: 0.0194197 +Time = 0.0005675 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 9083 + Current mass in system = 9.08723e-10 + Linear momentum = (2.82238e-11 -8.66497e-09 0) + |Linear momentum| = 8.66502e-09 + Linear kinetic energy = 4.39116e-08 + model1: + number of parcels added = 9091 + mass introduced = 9.22819e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.145, 511.203 + Mass transfer phase change = 1.40958e-11 + D10, D32, Dmax (mu) = 50.5272, 79.0437, 149.307 + Liquid penetration 95% mass (m) = 0.00458023 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0037494, Final residual = 5.70965e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0148553, Final residual = 3.99806e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00270408, Final residual = 2.01966e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00299652, Final residual = 1.42009e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00323759, Final residual = 1.76306e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0032376, Final residual = 1.76453e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0023401, Final residual = 1.47682e-07, No Iterations 1 +min/max(T) = 625.005, 853.417 +GAMG: Solving for p, Initial residual = 0.0338447, Final residual = 0.000510497, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.71433e-06, global = 1.68352e-06, cumulative = 0.000324796 +GAMG: Solving for p, Initial residual = 0.000500933, Final residual = 8.33929e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.68548e-06, global = 1.68543e-06, cumulative = 0.000326481 +smoothSolver: Solving for epsilon, Initial residual = 0.00113899, Final residual = 2.00158e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00406822, Final residual = 6.92116e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.06868 s +other Time = 0 s +rho Equations = 0.000191 s +U Equations = 0.000963 s +Y Equations = 0.00242386 s +E Equations = 0.000528 s +p Equations = 0.00199 s +calculate parcels = 15.236 s +chemistry correctThermo = 0.001916 s +turbulence correct = 0.000859 s +combustion correct(in Y) = 0.0596161 s +percentage of chemistry = 86.8028 % +percentage of rho/U/Y/E = 5.97825 % +========Time details of each equation======= +rhoEqn Time = 0.000315 s +rhoEqn assamble = 0.000252 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000962 s +UEqn assamble = 0.000609 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000353 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001504 s +YEqn assamble = 0.000591 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -2.7e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000385 s +EEqn assamble = 0.000286 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 34.92 s ClockTime = 35 s +Courant Number mean: 0.000249346 max: 0.0194542 +Time = 0.00057 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 56 new parcels + +Cloud: sprayCloud + Current number of parcels = 9139 + Current mass in system = 9.1315e-10 + Linear momentum = (2.80555e-11 -8.70007e-09 0) + |Linear momentum| = 8.70011e-09 + Linear kinetic energy = 4.40527e-08 + model1: + number of parcels added = 9147 + mass introduced = 9.27393e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.146, 511.267 + Mass transfer phase change = 1.42429e-11 + D10, D32, Dmax (mu) = 50.5759, 79.092, 149.313 + Liquid penetration 95% mass (m) = 0.00459712 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00364843, Final residual = 5.447e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0146803, Final residual = 3.98656e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00269802, Final residual = 1.97797e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00298752, Final residual = 1.42012e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00322751, Final residual = 1.7566e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00322753, Final residual = 1.75807e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00233564, Final residual = 1.4393e-07, No Iterations 1 +min/max(T) = 624.879, 853.81 +GAMG: Solving for p, Initial residual = 0.0347515, Final residual = 0.000437437, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.72227e-06, global = 1.69346e-06, cumulative = 0.000328175 +GAMG: Solving for p, Initial residual = 0.000425773, Final residual = 4.91199e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.69603e-06, global = 1.696e-06, cumulative = 0.000329871 +smoothSolver: Solving for epsilon, Initial residual = 0.00114229, Final residual = 2.01032e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00405102, Final residual = 6.90084e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.08304 s +other Time = 0 s +rho Equations = 0.000166 s +U Equations = 0.001163 s +Y Equations = 0.00228457 s +E Equations = 0.000492 s +p Equations = 0.001806 s +calculate parcels = 15.3802 s +chemistry correctThermo = 0.001996 s +turbulence correct = 0.000818 s +combustion correct(in Y) = 0.0741294 s +percentage of chemistry = 89.2695 % +percentage of rho/U/Y/E = 4.94409 % +========Time details of each equation======= +rhoEqn Time = 0.000284 s +rhoEqn assamble = 0.000228 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001162 s +UEqn assamble = 0.000714 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000448 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001636 s +YEqn assamble = 0.00061 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000163 s +YEqn correct boundary = 0 s +EEqn Time = 0.000373 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 35.15 s ClockTime = 36 s +Courant Number mean: 0.000250665 max: 0.0194654 +Time = 0.0005725 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 45 new parcels + +Cloud: sprayCloud + Current number of parcels = 9184 + Current mass in system = 9.16668e-10 + Linear momentum = (2.74441e-11 -8.72397e-09 0) + |Linear momentum| = 8.72401e-09 + Linear kinetic energy = 4.41242e-08 + model1: + number of parcels added = 9192 + mass introduced = 9.31059e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.142, 511.332 + Mass transfer phase change = 1.4391e-11 + D10, D32, Dmax (mu) = 50.594, 79.1195, 149.319 + Liquid penetration 95% mass (m) = 0.00461478 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00344445, Final residual = 5.05892e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0143873, Final residual = 3.94917e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00267864, Final residual = 1.95244e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00297859, Final residual = 1.41396e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0032177, Final residual = 1.75015e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00321772, Final residual = 1.75161e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00233702, Final residual = 1.42445e-07, No Iterations 1 +min/max(T) = 624.758, 854.204 +GAMG: Solving for p, Initial residual = 0.0363979, Final residual = 0.000454157, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.73215e-06, global = 1.70352e-06, cumulative = 0.000331574 +GAMG: Solving for p, Initial residual = 0.000442088, Final residual = 4.46258e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.70632e-06, global = 1.70629e-06, cumulative = 0.000333281 +smoothSolver: Solving for epsilon, Initial residual = 0.00114558, Final residual = 2.01891e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00403394, Final residual = 6.8797e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094542 s +other Time = 0 s +rho Equations = 0.000161 s +U Equations = 0.001133 s +Y Equations = 0.0020726 s +E Equations = 0.00053 s +p Equations = 0.001914 s +calculate parcels = 15.5377 s +chemistry correctThermo = 0.001971 s +turbulence correct = 0.000971 s +combustion correct(in Y) = 0.0855964 s +percentage of chemistry = 90.538 % +percentage of rho/U/Y/E = 4.12156 % +========Time details of each equation======= +rhoEqn Time = 0.000291 s +rhoEqn assamble = 0.000227 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001131 s +UEqn assamble = 0.000693 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000438 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001428 s +YEqn assamble = 0.000554 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.9e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000408 s +EEqn assamble = 0.000305 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000103 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 35.4 s ClockTime = 36 s +Courant Number mean: 0.00025225 max: 0.0194911 +Time = 0.000575 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 56 new parcels + +Cloud: sprayCloud + Current number of parcels = 9240 + Current mass in system = 9.21049e-10 + Linear momentum = (2.75681e-11 -8.75805e-09 0) + |Linear momentum| = 8.75809e-09 + Linear kinetic energy = 4.42569e-08 + model1: + number of parcels added = 9248 + mass introduced = 9.35589e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.149, 511.399 + Mass transfer phase change = 1.45399e-11 + D10, D32, Dmax (mu) = 50.6098, 79.1787, 149.325 + Liquid penetration 95% mass (m) = 0.00463358 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0034483, Final residual = 5.05628e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0140386, Final residual = 3.85868e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00267108, Final residual = 1.9135e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00296984, Final residual = 1.40151e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00320785, Final residual = 1.74422e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00320787, Final residual = 1.74567e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00233774, Final residual = 1.40197e-07, No Iterations 1 +min/max(T) = 624.621, 854.599 +GAMG: Solving for p, Initial residual = 0.0378985, Final residual = 0.000487311, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.74551e-06, global = 1.71422e-06, cumulative = 0.000334995 +GAMG: Solving for p, Initial residual = 0.000475244, Final residual = 3.79989e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.71678e-06, global = 1.71676e-06, cumulative = 0.000336712 +smoothSolver: Solving for epsilon, Initial residual = 0.00114861, Final residual = 2.02716e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00401639, Final residual = 6.85721e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.086673 s +other Time = 0 s +rho Equations = 0.000166 s +U Equations = 0.001108 s +Y Equations = 0.00206375 s +E Equations = 0.000554 s +p Equations = 0.001838 s +calculate parcels = 15.7044 s +chemistry correctThermo = 0.001972 s +turbulence correct = 0.000822 s +combustion correct(in Y) = 0.0779583 s +percentage of chemistry = 89.9453 % +percentage of rho/U/Y/E = 4.49015 % +========Time details of each equation======= +rhoEqn Time = 0.000286 s +rhoEqn assamble = 0.000229 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001107 s +UEqn assamble = 0.000678 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000429 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001423 s +YEqn assamble = 0.000536 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.3e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000432 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000149 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 35.65 s ClockTime = 36 s +Courant Number mean: 0.000254172 max: 0.0195278 +Time = 0.0005775 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 54 new parcels + +Cloud: sprayCloud + Current number of parcels = 9294 + Current mass in system = 9.25257e-10 + Linear momentum = (2.68931e-11 -8.78985e-09 0) + |Linear momentum| = 8.7899e-09 + Linear kinetic energy = 4.43744e-08 + model1: + number of parcels added = 9302 + mass introduced = 9.39946e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.138, 511.467 + Mass transfer phase change = 1.46899e-11 + D10, D32, Dmax (mu) = 50.6449, 79.217, 149.331 + Liquid penetration 95% mass (m) = 0.00465016 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00352835, Final residual = 5.29098e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0136344, Final residual = 3.74674e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00265807, Final residual = 1.86208e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00296106, Final residual = 1.38834e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00319711, Final residual = 1.73932e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00319713, Final residual = 1.74076e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00233361, Final residual = 1.36047e-07, No Iterations 1 +min/max(T) = 624.465, 854.996 +GAMG: Solving for p, Initial residual = 0.0398967, Final residual = 0.000508523, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.75671e-06, global = 1.72469e-06, cumulative = 0.000338436 +GAMG: Solving for p, Initial residual = 0.000499393, Final residual = 4.45378e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.72797e-06, global = 1.72794e-06, cumulative = 0.000340164 +smoothSolver: Solving for epsilon, Initial residual = 0.00115155, Final residual = 2.03476e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00399943, Final residual = 6.83503e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102801 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001114 s +Y Equations = 0.00339929 s +E Equations = 0.000938 s +p Equations = 0.00188 s +calculate parcels = 15.8587 s +chemistry correctThermo = 0.004927 s +turbulence correct = 0.000838 s +combustion correct(in Y) = 0.0893257 s +percentage of chemistry = 86.8919 % +percentage of rho/U/Y/E = 5.47493 % +========Time details of each equation======= +rhoEqn Time = 0.0003 s +rhoEqn assamble = 0.000238 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001112 s +UEqn assamble = 0.000685 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000427 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002746 s +YEqn assamble = 0.000953 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000551 s +YEqn correct boundary = 0 s +EEqn Time = 0.000704 s +EEqn assamble = 0.000507 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000197 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 35.91 s ClockTime = 36 s +Courant Number mean: 0.000256196 max: 0.0195296 +Time = 0.00058 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 54 new parcels + +Cloud: sprayCloud + Current number of parcels = 9348 + Current mass in system = 9.29448e-10 + Linear momentum = (2.6045e-11 -8.82132e-09 0) + |Linear momentum| = 8.82136e-09 + Linear kinetic energy = 4.44883e-08 + model1: + number of parcels added = 9356 + mass introduced = 9.44289e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.139, 511.537 + Mass transfer phase change = 1.48407e-11 + D10, D32, Dmax (mu) = 50.6789, 79.2548, 149.337 + Liquid penetration 95% mass (m) = 0.0046677 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00341962, Final residual = 5.06022e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.013272, Final residual = 3.67375e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00265595, Final residual = 1.8153e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00295248, Final residual = 1.37761e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00318699, Final residual = 1.73405e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00318701, Final residual = 1.73549e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00233519, Final residual = 1.33136e-07, No Iterations 1 +min/max(T) = 624.293, 855.392 +GAMG: Solving for p, Initial residual = 0.0402971, Final residual = 0.000464794, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.76598e-06, global = 1.73475e-06, cumulative = 0.000341899 +GAMG: Solving for p, Initial residual = 0.000451731, Final residual = 5.73316e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.73882e-06, global = 1.73878e-06, cumulative = 0.000343638 +smoothSolver: Solving for epsilon, Initial residual = 0.00115443, Final residual = 2.04206e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0039829, Final residual = 6.81256e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.096144 s +other Time = 1e-06 s +rho Equations = 0.000179 s +U Equations = 0.001117 s +Y Equations = 0.002405 s +E Equations = 0.000611 s +p Equations = 0.002432 s +calculate parcels = 16.0146 s +chemistry correctThermo = 0.002778 s +turbulence correct = 0.001032 s +combustion correct(in Y) = 0.085395 s +percentage of chemistry = 88.8199 % +percentage of rho/U/Y/E = 4.48494 % +========Time details of each equation======= +rhoEqn Time = 0.000351 s +rhoEqn assamble = 0.000265 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001116 s +UEqn assamble = 0.000686 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00043 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001766 s +YEqn assamble = 0.000663 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000184 s +YEqn correct boundary = 0 s +EEqn Time = 0.000456 s +EEqn assamble = 0.000341 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 36.16 s ClockTime = 37 s +Courant Number mean: 0.000258236 max: 0.0195379 +Time = 0.0005825 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 41 new parcels + +Cloud: sprayCloud + Current number of parcels = 9389 + Current mass in system = 9.32582e-10 + Linear momentum = (2.5822e-11 -8.84e-09 0) + |Linear momentum| = 8.84004e-09 + Linear kinetic energy = 4.4525e-08 + model1: + number of parcels added = 9397 + mass introduced = 9.47575e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.155, 511.606 + Mass transfer phase change = 1.49925e-11 + D10, D32, Dmax (mu) = 50.6191, 79.245, 149.343 + Liquid penetration 95% mass (m) = 0.00468422 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00337953, Final residual = 4.83512e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0129436, Final residual = 3.60849e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00265017, Final residual = 1.78379e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00294316, Final residual = 1.36562e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00317598, Final residual = 1.7285e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.003176, Final residual = 1.72992e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00233295, Final residual = 1.32061e-07, No Iterations 1 +min/max(T) = 624.105, 855.791 +GAMG: Solving for p, Initial residual = 0.0412636, Final residual = 0.000413433, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.77184e-06, global = 1.74578e-06, cumulative = 0.000345384 +GAMG: Solving for p, Initial residual = 0.000407127, Final residual = 4.44378e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.74906e-06, global = 1.74903e-06, cumulative = 0.000347133 +smoothSolver: Solving for epsilon, Initial residual = 0.00115688, Final residual = 2.04849e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.003966, Final residual = 6.78869e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.08982 s +other Time = 0 s +rho Equations = 0.000174 s +U Equations = 0.001161 s +Y Equations = 0.00202098 s +E Equations = 0.000495 s +p Equations = 0.001976 s +calculate parcels = 16.1714 s +chemistry correctThermo = 0.001975 s +turbulence correct = 0.000935 s +combustion correct(in Y) = 0.080891 s +percentage of chemistry = 90.059 % +percentage of rho/U/Y/E = 4.28744 % +========Time details of each equation======= +rhoEqn Time = 0.000313 s +rhoEqn assamble = 0.000247 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001161 s +UEqn assamble = 0.000718 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000443 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001372 s +YEqn assamble = 0.000526 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.2e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000378 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 36.41 s ClockTime = 37 s +Courant Number mean: 0.000260296 max: 0.0195555 +Time = 0.000585 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 53 new parcels + +Cloud: sprayCloud + Current number of parcels = 9442 + Current mass in system = 9.36638e-10 + Linear momentum = (2.6448e-11 -8.86922e-09 0) + |Linear momentum| = 8.86926e-09 + Linear kinetic energy = 4.46241e-08 + model1: + number of parcels added = 9450 + mass introduced = 9.51784e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.141, 511.676 + Mass transfer phase change = 1.51453e-11 + D10, D32, Dmax (mu) = 48.9736, 79.2142, 149.349 + Liquid penetration 95% mass (m) = 0.00470245 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00330514, Final residual = 4.68698e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0125672, Final residual = 3.52215e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00262952, Final residual = 1.72079e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00293528, Final residual = 1.36051e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00316527, Final residual = 1.72241e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00316529, Final residual = 1.72382e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00231852, Final residual = 1.29578e-07, No Iterations 1 +min/max(T) = 623.906, 856.189 +GAMG: Solving for p, Initial residual = 0.0421418, Final residual = 0.000671927, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.80001e-06, global = 1.75669e-06, cumulative = 0.000348889 +GAMG: Solving for p, Initial residual = 0.000662146, Final residual = 2.1199e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.76181e-06, global = 1.7618e-06, cumulative = 0.000350651 +smoothSolver: Solving for epsilon, Initial residual = 0.001158, Final residual = 2.05229e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00394764, Final residual = 6.76015e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.072575 s +other Time = 1e-06 s +rho Equations = 0.000147 s +U Equations = 0.000972 s +Y Equations = 0.0023785 s +E Equations = 0.000601 s +p Equations = 0.002391 s +calculate parcels = 16.3391 s +chemistry correctThermo = 0.002794 s +turbulence correct = 0.001041 s +combustion correct(in Y) = 0.0620805 s +percentage of chemistry = 85.5398 % +percentage of rho/U/Y/E = 5.64725 % +========Time details of each equation======= +rhoEqn Time = 0.000306 s +rhoEqn assamble = 0.000242 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000972 s +UEqn assamble = 0.000596 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000376 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001805 s +YEqn assamble = 0.00064 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000219 s +YEqn correct boundary = 0 s +EEqn Time = 0.000447 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 36.65 s ClockTime = 37 s +Courant Number mean: 0.000262474 max: 0.019553 +Time = 0.0005875 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 9493 + Current mass in system = 9.40517e-10 + Linear momentum = (2.71874e-11 -8.89626e-09 0) + |Linear momentum| = 8.8963e-09 + Linear kinetic energy = 4.47087e-08 + model1: + number of parcels added = 9501 + mass introduced = 9.55816e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.153, 511.745 + Mass transfer phase change = 1.52992e-11 + D10, D32, Dmax (mu) = 49.0248, 79.2542, 149.355 + Liquid penetration 95% mass (m) = 0.00471851 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00357706, Final residual = 5.05635e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0121794, Final residual = 3.33834e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00261915, Final residual = 1.70572e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00292638, Final residual = 1.35285e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00315452, Final residual = 1.71534e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00315454, Final residual = 1.71675e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00231195, Final residual = 1.27649e-07, No Iterations 1 +min/max(T) = 623.719, 856.583 +GAMG: Solving for p, Initial residual = 0.0441656, Final residual = 0.000739732, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.81483e-06, global = 1.76708e-06, cumulative = 0.000352418 +GAMG: Solving for p, Initial residual = 0.000728414, Final residual = 7.47342e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.77381e-06, global = 1.77376e-06, cumulative = 0.000354192 +smoothSolver: Solving for epsilon, Initial residual = 0.00115936, Final residual = 2.05616e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00392954, Final residual = 6.73154e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09734 s +other Time = 0 s +rho Equations = 0.000161 s +U Equations = 0.001104 s +Y Equations = 0.00251126 s +E Equations = 0.000643 s +p Equations = 0.002292 s +calculate parcels = 16.4885 s +chemistry correctThermo = 0.002804 s +turbulence correct = 0.001009 s +combustion correct(in Y) = 0.0866237 s +percentage of chemistry = 88.9909 % +percentage of rho/U/Y/E = 4.54003 % +========Time details of each equation======= +rhoEqn Time = 0.000312 s +rhoEqn assamble = 0.000248 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001102 s +UEqn assamble = 0.000671 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000431 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001881 s +YEqn assamble = 0.000738 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000197 s +YEqn correct boundary = 0 s +EEqn Time = 0.000485 s +EEqn assamble = 0.000361 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000124 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 36.89 s ClockTime = 37 s +Courant Number mean: 0.000264708 max: 0.0195444 +Time = 0.00059 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 56 new parcels + +Cloud: sprayCloud + Current number of parcels = 9549 + Current mass in system = 9.44767e-10 + Linear momentum = (2.71868e-11 -8.92744e-09 0) + |Linear momentum| = 8.92748e-09 + Linear kinetic energy = 4.48162e-08 + model1: + number of parcels added = 9557 + mass introduced = 9.60222e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.137, 511.815 + Mass transfer phase change = 1.54542e-11 + D10, D32, Dmax (mu) = 49.0774, 79.2961, 149.361 + Liquid penetration 95% mass (m) = 0.00473344 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00366652, Final residual = 5.37838e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0118748, Final residual = 3.21721e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00260086, Final residual = 1.66574e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00291708, Final residual = 1.34918e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00314245, Final residual = 1.70851e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00314247, Final residual = 1.7099e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00230243, Final residual = 1.2636e-07, No Iterations 1 +min/max(T) = 623.544, 856.98 +GAMG: Solving for p, Initial residual = 0.0433982, Final residual = 0.000499947, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.81813e-06, global = 1.78161e-06, cumulative = 0.000355974 +GAMG: Solving for p, Initial residual = 0.000483628, Final residual = 6.41434e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.78638e-06, global = 1.78633e-06, cumulative = 0.00035776 +smoothSolver: Solving for epsilon, Initial residual = 0.00116071, Final residual = 2.05947e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00391171, Final residual = 6.70253e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.068276 s +other Time = 0 s +rho Equations = 0.000166 s +U Equations = 0.001018 s +Y Equations = 0.0021448 s +E Equations = 0.000493 s +p Equations = 0.001936 s +calculate parcels = 16.6561 s +chemistry correctThermo = 0.001987 s +turbulence correct = 0.000904 s +combustion correct(in Y) = 0.0594362 s +percentage of chemistry = 87.0528 % +percentage of rho/U/Y/E = 5.59758 % +========Time details of each equation======= +rhoEqn Time = 0.000288 s +rhoEqn assamble = 0.000232 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001017 s +UEqn assamble = 0.000639 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000378 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001538 s +YEqn assamble = 0.000578 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000118 s +YEqn correct boundary = 0 s +EEqn Time = 0.000371 s +EEqn assamble = 0.00028 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 37.13 s ClockTime = 38 s +Courant Number mean: 0.00026695 max: 0.0195374 +Time = 0.0005925 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 45 new parcels + +Cloud: sprayCloud + Current number of parcels = 9594 + Current mass in system = 9.4814e-10 + Linear momentum = (2.64266e-11 -8.94819e-09 0) + |Linear momentum| = 8.94823e-09 + Linear kinetic energy = 4.48617e-08 + model1: + number of parcels added = 9602 + mass introduced = 9.63751e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.149, 511.884 + Mass transfer phase change = 1.56103e-11 + D10, D32, Dmax (mu) = 49.1155, 79.3206, 149.366 + Liquid penetration 95% mass (m) = 0.00475269 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00375516, Final residual = 5.46732e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0116998, Final residual = 3.14891e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00259701, Final residual = 1.57556e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00290846, Final residual = 1.35483e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00313173, Final residual = 1.70083e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00313175, Final residual = 1.70221e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00229388, Final residual = 1.27363e-07, No Iterations 1 +min/max(T) = 623.356, 857.378 +GAMG: Solving for p, Initial residual = 0.0436367, Final residual = 0.000491243, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.83043e-06, global = 1.79528e-06, cumulative = 0.000359555 +GAMG: Solving for p, Initial residual = 0.000474889, Final residual = 8.63149e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.79901e-06, global = 1.79895e-06, cumulative = 0.000361354 +smoothSolver: Solving for epsilon, Initial residual = 0.00116213, Final residual = 2.06299e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00389427, Final residual = 6.67414e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.069688 s +other Time = 1e-06 s +rho Equations = 0.000162 s +U Equations = 0.000958 s +Y Equations = 0.00214108 s +E Equations = 0.000491 s +p Equations = 0.001965 s +calculate parcels = 16.7775 s +chemistry correctThermo = 0.001909 s +turbulence correct = 0.000853 s +combustion correct(in Y) = 0.0610339 s +percentage of chemistry = 87.5817 % +percentage of rho/U/Y/E = 5.38411 % +========Time details of each equation======= +rhoEqn Time = 0.000289 s +rhoEqn assamble = 0.000231 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000957 s +UEqn assamble = 0.000598 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000359 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001573 s +YEqn assamble = 0.000573 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000153 s +YEqn correct boundary = 0 s +EEqn Time = 0.000366 s +EEqn assamble = 0.000274 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 37.32 s ClockTime = 38 s +Courant Number mean: 0.000269122 max: 0.019532 +Time = 0.000595 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 54 new parcels + +Cloud: sprayCloud + Current number of parcels = 9648 + Current mass in system = 9.52185e-10 + Linear momentum = (2.73804e-11 -8.9764e-09 0) + |Linear momentum| = 8.97644e-09 + Linear kinetic energy = 4.4949e-08 + model1: + number of parcels added = 9656 + mass introduced = 9.67952e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.147, 511.955 + Mass transfer phase change = 1.57679e-11 + D10, D32, Dmax (mu) = 48.2946, 79.2816, 149.372 + Liquid penetration 95% mass (m) = 0.00477133 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00383901, Final residual = 5.4444e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0115707, Final residual = 3.12021e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00258177, Final residual = 1.56715e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00290232, Final residual = 1.35708e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0031197, Final residual = 1.69256e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00311971, Final residual = 1.69393e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00230232, Final residual = 1.30553e-07, No Iterations 1 +min/max(T) = 623.172, 857.777 +GAMG: Solving for p, Initial residual = 0.04454, Final residual = 0.000801563, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.86456e-06, global = 1.8098e-06, cumulative = 0.000363164 +GAMG: Solving for p, Initial residual = 0.000783627, Final residual = 3.20215e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.81655e-06, global = 1.81653e-06, cumulative = 0.00036498 +smoothSolver: Solving for epsilon, Initial residual = 0.00116195, Final residual = 2.06314e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00387553, Final residual = 6.64066e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.091374 s +other Time = 0 s +rho Equations = 0.000171 s +U Equations = 0.001115 s +Y Equations = 0.00250776 s +E Equations = 0.000607 s +p Equations = 0.002508 s +calculate parcels = 16.9292 s +chemistry correctThermo = 0.002823 s +turbulence correct = 0.001004 s +combustion correct(in Y) = 0.0804452 s +percentage of chemistry = 88.0395 % +percentage of rho/U/Y/E = 4.81621 % +========Time details of each equation======= +rhoEqn Time = 0.000322 s +rhoEqn assamble = 0.000256 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001115 s +UEqn assamble = 0.00068 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000435 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001871 s +YEqn assamble = 0.00066 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000216 s +YEqn correct boundary = 0 s +EEqn Time = 0.000448 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 37.56 s ClockTime = 38 s +Courant Number mean: 0.000271337 max: 0.0194975 +Time = 0.0005975 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 47 new parcels + +Cloud: sprayCloud + Current number of parcels = 9695 + Current mass in system = 9.55668e-10 + Linear momentum = (2.82128e-11 -8.99792e-09 0) + |Linear momentum| = 8.99796e-09 + Linear kinetic energy = 4.49966e-08 + model1: + number of parcels added = 9703 + mass introduced = 9.71595e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.135, 512.026 + Mass transfer phase change = 1.59266e-11 + D10, D32, Dmax (mu) = 48.2804, 79.274, 149.378 + Liquid penetration 95% mass (m) = 0.00479087 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00418396, Final residual = 5.61816e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.011397, Final residual = 3.02626e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00257062, Final residual = 1.54091e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00289348, Final residual = 1.35862e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00310845, Final residual = 1.68303e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00310846, Final residual = 1.68439e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00229579, Final residual = 1.31194e-07, No Iterations 1 +min/max(T) = 622.992, 858.167 +GAMG: Solving for p, Initial residual = 0.0443484, Final residual = 0.000625774, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.86624e-06, global = 1.82476e-06, cumulative = 0.000366805 +GAMG: Solving for p, Initial residual = 0.000610007, Final residual = 1.67556e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.82965e-06, global = 1.82964e-06, cumulative = 0.000368635 +smoothSolver: Solving for epsilon, Initial residual = 0.00116287, Final residual = 2.06493e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00385782, Final residual = 6.60894e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.110149 s +other Time = 1e-06 s +rho Equations = 0.000192 s +U Equations = 0.001226 s +Y Equations = 0.0027169 s +E Equations = 0.000676 s +p Equations = 0.00285 s +calculate parcels = 17.0771 s +chemistry correctThermo = 0.003068 s +turbulence correct = 0.001183 s +combustion correct(in Y) = 0.0980401 s +percentage of chemistry = 89.0068 % +percentage of rho/U/Y/E = 4.36763 % +========Time details of each equation======= +rhoEqn Time = 0.000401 s +rhoEqn assamble = 0.000321 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001225 s +UEqn assamble = 0.000748 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000477 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001966 s +YEqn assamble = 0.000734 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000195 s +YEqn correct boundary = 0 s +EEqn Time = 0.000505 s +EEqn assamble = 0.000373 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000132 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 37.82 s ClockTime = 38 s +Courant Number mean: 0.000273418 max: 0.0194891 +Time = 0.0006 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 47 new parcels + +Cloud: sprayCloud + Current number of parcels = 9742 + Current mass in system = 9.59125e-10 + Linear momentum = (2.84347e-11 -9.01891e-09 0) + |Linear momentum| = 9.01896e-09 + Linear kinetic energy = 4.50405e-08 + model1: + number of parcels added = 9750 + mass introduced = 9.75212e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.133, 512.097 + Mass transfer phase change = 1.60865e-11 + D10, D32, Dmax (mu) = 48.317, 79.2946, 149.384 + Liquid penetration 95% mass (m) = 0.00480661 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00397722, Final residual = 5.55319e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0111201, Final residual = 2.93893e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00256561, Final residual = 1.51393e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00288476, Final residual = 1.36264e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00309653, Final residual = 1.67312e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00309654, Final residual = 1.67446e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00228816, Final residual = 1.32139e-07, No Iterations 1 +min/max(T) = 622.806, 858.565 +GAMG: Solving for p, Initial residual = 0.0424076, Final residual = 0.000604691, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.8846e-06, global = 1.83626e-06, cumulative = 0.000370471 +GAMG: Solving for p, Initial residual = 0.000581321, Final residual = 1.62895e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.84347e-06, global = 1.84346e-06, cumulative = 0.000372315 +smoothSolver: Solving for epsilon, Initial residual = 0.00116437, Final residual = 2.06784e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00384084, Final residual = 6.5792e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094208 s +other Time = 1e-06 s +rho Equations = 0.000166 s +U Equations = 0.001147 s +Y Equations = 0.00209471 s +E Equations = 0.000502 s +p Equations = 0.002361 s +calculate parcels = 17.2215 s +chemistry correctThermo = 0.002024 s +turbulence correct = 0.001033 s +combustion correct(in Y) = 0.0847003 s +percentage of chemistry = 89.9077 % +percentage of rho/U/Y/E = 4.15009 % +========Time details of each equation======= +rhoEqn Time = 0.000301 s +rhoEqn assamble = 0.000236 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001146 s +UEqn assamble = 0.000698 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000448 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001389 s +YEqn assamble = 0.000535 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 6.9e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000379 s +EEqn assamble = 0.000285 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 38.24 s ClockTime = 39 s +Courant Number mean: 0.000275312 max: 0.0195007 +Time = 0.0006025 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 67 new parcels + +Cloud: sprayCloud + Current number of parcels = 9809 + Current mass in system = 9.64084e-10 + Linear momentum = (2.78425e-11 -9.05674e-09 0) + |Linear momentum| = 9.05679e-09 + Linear kinetic energy = 4.51796e-08 + model1: + number of parcels added = 9817 + mass introduced = 9.80332e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.132, 512.168 + Mass transfer phase change = 1.62477e-11 + D10, D32, Dmax (mu) = 48.366, 79.348, 149.594 + Liquid penetration 95% mass (m) = 0.00482377 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0037739, Final residual = 5.26387e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0109316, Final residual = 2.92514e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00255639, Final residual = 1.51734e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00287674, Final residual = 1.36644e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00308579, Final residual = 1.66349e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00308581, Final residual = 1.66482e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00228269, Final residual = 1.32459e-07, No Iterations 1 +min/max(T) = 622.613, 859.233 +GAMG: Solving for p, Initial residual = 0.0413762, Final residual = 0.000531098, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.89633e-06, global = 1.85276e-06, cumulative = 0.000374167 +GAMG: Solving for p, Initial residual = 0.000511996, Final residual = 6.82527e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.85779e-06, global = 1.85773e-06, cumulative = 0.000376025 +smoothSolver: Solving for epsilon, Initial residual = 0.00116494, Final residual = 2.06907e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00382332, Final residual = 6.548e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097905 s +other Time = 0 s +rho Equations = 0.00017 s +U Equations = 0.001099 s +Y Equations = 0.00241489 s +E Equations = 0.000661 s +p Equations = 0.002319 s +calculate parcels = 17.4062 s +chemistry correctThermo = 0.002761 s +turbulence correct = 0.001 s +combustion correct(in Y) = 0.0872871 s +percentage of chemistry = 89.1549 % +percentage of rho/U/Y/E = 4.43786 % +========Time details of each equation======= +rhoEqn Time = 0.000319 s +rhoEqn assamble = 0.000253 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001099 s +UEqn assamble = 0.000674 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000425 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00177 s +YEqn assamble = 0.000685 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000186 s +YEqn correct boundary = 0 s +EEqn Time = 0.000499 s +EEqn assamble = 0.000365 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000134 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 38.53 s ClockTime = 39 s +Courant Number mean: 0.000277102 max: 0.0194966 +Time = 0.000605 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 9857 + Current mass in system = 9.67595e-10 + Linear momentum = (2.80481e-11 -9.07804e-09 0) + |Linear momentum| = 9.07808e-09 + Linear kinetic energy = 4.5223e-08 + model1: + number of parcels added = 9865 + mass introduced = 9.84005e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.131, 512.239 + Mass transfer phase change = 1.64101e-11 + D10, D32, Dmax (mu) = 48.3919, 79.3973, 149.395 + Liquid penetration 95% mass (m) = 0.00484056 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00338186, Final residual = 4.89515e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0106713, Final residual = 2.88164e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00256389, Final residual = 1.50104e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00286724, Final residual = 1.3705e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00307427, Final residual = 1.65421e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00307429, Final residual = 1.65554e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0022714, Final residual = 1.33349e-07, No Iterations 1 +min/max(T) = 622.405, 859.975 +GAMG: Solving for p, Initial residual = 0.0393584, Final residual = 0.0004381, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.90575e-06, global = 1.86613e-06, cumulative = 0.000377891 +GAMG: Solving for p, Initial residual = 0.000421509, Final residual = 5.67168e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.87109e-06, global = 1.87104e-06, cumulative = 0.000379762 +smoothSolver: Solving for epsilon, Initial residual = 0.00116569, Final residual = 2.07073e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00380602, Final residual = 6.51712e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092895 s +other Time = 0 s +rho Equations = 0.000157 s +U Equations = 0.001162 s +Y Equations = 0.00242181 s +E Equations = 0.000611 s +p Equations = 0.002181 s +calculate parcels = 17.553 s +chemistry correctThermo = 0.002778 s +turbulence correct = 0.001001 s +combustion correct(in Y) = 0.0823712 s +percentage of chemistry = 88.6713 % +percentage of rho/U/Y/E = 4.68466 % +========Time details of each equation======= +rhoEqn Time = 0.000298 s +rhoEqn assamble = 0.000234 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001162 s +UEqn assamble = 0.000728 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000434 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001757 s +YEqn assamble = 0.000655 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000187 s +YEqn correct boundary = 0 s +EEqn Time = 0.000456 s +EEqn assamble = 0.000343 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 38.77 s ClockTime = 39 s +Courant Number mean: 0.000278758 max: 0.0194919 +Time = 0.0006075 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 9906 + Current mass in system = 9.71157e-10 + Linear momentum = (2.88538e-11 -9.09966e-09 0) + |Linear momentum| = 9.09971e-09 + Linear kinetic energy = 4.52677e-08 + model1: + number of parcels added = 9914 + mass introduced = 9.8773e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.143, 512.308 + Mass transfer phase change = 1.65736e-11 + D10, D32, Dmax (mu) = 48.3936, 79.4091, 149.401 + Liquid penetration 95% mass (m) = 0.00485755 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00316112, Final residual = 4.58963e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0103692, Final residual = 2.83362e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00254912, Final residual = 1.50769e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00285848, Final residual = 1.36675e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00306341, Final residual = 1.64953e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00306343, Final residual = 1.65086e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00226143, Final residual = 1.33494e-07, No Iterations 1 +min/max(T) = 622.206, 860.724 +GAMG: Solving for p, Initial residual = 0.0382896, Final residual = 0.000410162, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.9169e-06, global = 1.88119e-06, cumulative = 0.000381643 +GAMG: Solving for p, Initial residual = 0.000393786, Final residual = 4.60761e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.88467e-06, global = 1.88464e-06, cumulative = 0.000383528 +smoothSolver: Solving for epsilon, Initial residual = 0.00116605, Final residual = 2.07149e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00378796, Final residual = 6.48431e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.093599 s +other Time = 0 s +rho Equations = 0.000153 s +U Equations = 0.000962 s +Y Equations = 0.00235046 s +E Equations = 0.000626 s +p Equations = 0.002171 s +calculate parcels = 17.7074 s +chemistry correctThermo = 0.002783 s +turbulence correct = 0.000944 s +combustion correct(in Y) = 0.0834115 s +percentage of chemistry = 89.1158 % +percentage of rho/U/Y/E = 4.37126 % +========Time details of each equation======= +rhoEqn Time = 0.000293 s +rhoEqn assamble = 0.000233 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000961 s +UEqn assamble = 0.000605 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000356 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001788 s +YEqn assamble = 0.000666 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000209 s +YEqn correct boundary = 0 s +EEqn Time = 0.000472 s +EEqn assamble = 0.000355 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 39.02 s ClockTime = 39 s +Courant Number mean: 0.00028038 max: 0.0194808 +Time = 0.00061 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 55 new parcels + +Cloud: sprayCloud + Current number of parcels = 9961 + Current mass in system = 9.75147e-10 + Linear momentum = (2.89376e-11 -9.12586e-09 0) + |Linear momentum| = 9.1259e-09 + Linear kinetic energy = 4.5337e-08 + model1: + number of parcels added = 9969 + mass introduced = 9.91885e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.142, 513.883 + Mass transfer phase change = 1.67383e-11 + D10, D32, Dmax (mu) = 48.4165, 79.4407, 149.406 + Liquid penetration 95% mass (m) = 0.00487357 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00300516, Final residual = 4.68204e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0100309, Final residual = 2.74391e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.002541, Final residual = 1.49228e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00284966, Final residual = 1.36716e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00305264, Final residual = 1.64377e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00305265, Final residual = 1.64509e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00225176, Final residual = 1.33378e-07, No Iterations 1 +min/max(T) = 622.011, 861.48 +GAMG: Solving for p, Initial residual = 0.0370871, Final residual = 0.000402216, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.93048e-06, global = 1.8942e-06, cumulative = 0.000385422 +GAMG: Solving for p, Initial residual = 0.000384448, Final residual = 4.79011e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.89844e-06, global = 1.89841e-06, cumulative = 0.000387321 +smoothSolver: Solving for epsilon, Initial residual = 0.00116584, Final residual = 2.07161e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00376892, Final residual = 6.45011e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095882 s +other Time = 0 s +rho Equations = 0.000185 s +U Equations = 0.001166 s +Y Equations = 0.00252522 s +E Equations = 0.000659 s +p Equations = 0.002095 s +calculate parcels = 17.8671 s +chemistry correctThermo = 0.002769 s +turbulence correct = 0.000878 s +combustion correct(in Y) = 0.0854078 s +percentage of chemistry = 89.0759 % +percentage of rho/U/Y/E = 4.73 % +========Time details of each equation======= +rhoEqn Time = 0.000342 s +rhoEqn assamble = 0.000275 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001166 s +UEqn assamble = 0.000732 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000434 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00188 s +YEqn assamble = 0.000698 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000192 s +YEqn correct boundary = 0 s +EEqn Time = 0.000498 s +EEqn assamble = 0.000377 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000121 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 39.27 s ClockTime = 40 s +Courant Number mean: 0.000282064 max: 0.0194811 +Time = 0.0006125 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 72 new parcels + +Cloud: sprayCloud + Current number of parcels = 10033 + Current mass in system = 9.80399e-10 + Linear momentum = (2.88312e-11 -9.16573e-09 0) + |Linear momentum| = 9.16578e-09 + Linear kinetic energy = 4.54819e-08 + model1: + number of parcels added = 10041 + mass introduced = 9.97304e-10 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.146, 516.978 + Mass transfer phase change = 1.69043e-11 + D10, D32, Dmax (mu) = 48.458, 79.4948, 149.412 + Liquid penetration 95% mass (m) = 0.00489088 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00316935, Final residual = 5.17417e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00968722, Final residual = 2.62994e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00253638, Final residual = 1.50446e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00284235, Final residual = 1.37453e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00304278, Final residual = 1.63879e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0030428, Final residual = 1.64012e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00224763, Final residual = 1.34469e-07, No Iterations 1 +min/max(T) = 621.814, 862.241 +GAMG: Solving for p, Initial residual = 0.0365601, Final residual = 0.000404359, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.94877e-06, global = 1.90952e-06, cumulative = 0.00038923 +GAMG: Solving for p, Initial residual = 0.000390049, Final residual = 5.04956e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.91401e-06, global = 1.91397e-06, cumulative = 0.000391144 +smoothSolver: Solving for epsilon, Initial residual = 0.00116517, Final residual = 2.07057e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00374953, Final residual = 6.41447e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.075276 s +other Time = 1e-06 s +rho Equations = 0.00024 s +U Equations = 0.001341 s +Y Equations = 0.00226077 s +E Equations = 0.000544 s +p Equations = 0.001982 s +calculate parcels = 18.0334 s +chemistry correctThermo = 0.00204 s +turbulence correct = 0.000899 s +combustion correct(in Y) = 0.0656872 s +percentage of chemistry = 87.2619 % +percentage of rho/U/Y/E = 5.82625 % +========Time details of each equation======= +rhoEqn Time = 0.000371 s +rhoEqn assamble = 0.000294 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001339 s +UEqn assamble = 0.00084 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000499 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00149 s +YEqn assamble = 0.000572 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 5.3e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000419 s +EEqn assamble = 0.000316 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000103 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 39.51 s ClockTime = 40 s +Courant Number mean: 0.000283803 max: 0.0194705 +Time = 0.000615 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 54 new parcels + +Cloud: sprayCloud + Current number of parcels = 10087 + Current mass in system = 9.84311e-10 + Linear momentum = (2.92149e-11 -9.19052e-09 0) + |Linear momentum| = 9.19057e-09 + Linear kinetic energy = 4.55412e-08 + model1: + number of parcels added = 10095 + mass introduced = 1.00138e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.133, 519.785 + Mass transfer phase change = 1.70717e-11 + D10, D32, Dmax (mu) = 48.4946, 79.534, 149.418 + Liquid penetration 95% mass (m) = 0.00490789 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00367422, Final residual = 5.92338e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00940258, Final residual = 2.53858e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0025278, Final residual = 1.51078e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00283386, Final residual = 1.37888e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00303177, Final residual = 1.63504e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00303179, Final residual = 1.63636e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00224129, Final residual = 1.35212e-07, No Iterations 1 +min/max(T) = 621.632, 863.008 +GAMG: Solving for p, Initial residual = 0.0358943, Final residual = 0.000374736, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.96125e-06, global = 1.92423e-06, cumulative = 0.000393068 +GAMG: Solving for p, Initial residual = 0.000361174, Final residual = 3.28716e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.92893e-06, global = 1.9289e-06, cumulative = 0.000394997 +smoothSolver: Solving for epsilon, Initial residual = 0.00116483, Final residual = 2.06954e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00373057, Final residual = 6.37898e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.06887 s +other Time = 0 s +rho Equations = 0.000146 s +U Equations = 0.001008 s +Y Equations = 0.00238155 s +E Equations = 0.000489 s +p Equations = 0.002035 s +calculate parcels = 18.1635 s +chemistry correctThermo = 0.001897 s +turbulence correct = 0.000869 s +combustion correct(in Y) = 0.0598714 s +percentage of chemistry = 86.934 % +percentage of rho/U/Y/E = 5.84369 % +========Time details of each equation======= +rhoEqn Time = 0.000281 s +rhoEqn assamble = 0.000215 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001008 s +UEqn assamble = 0.000644 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000364 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001832 s +YEqn assamble = 0.000632 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000192 s +YEqn correct boundary = 0 s +EEqn Time = 0.000365 s +EEqn assamble = 0.000275 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 39.71 s ClockTime = 40 s +Courant Number mean: 0.000285553 max: 0.0194572 +Time = 0.0006175 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 10138 + Current mass in system = 9.87979e-10 + Linear momentum = (2.98768e-11 -9.21244e-09 0) + |Linear momentum| = 9.21249e-09 + Linear kinetic energy = 4.55833e-08 + model1: + number of parcels added = 10146 + mass introduced = 1.00522e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.128, 522.309 + Mass transfer phase change = 1.72403e-11 + D10, D32, Dmax (mu) = 48.3765, 79.5576, 149.423 + Liquid penetration 95% mass (m) = 0.00492441 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0039584, Final residual = 6.45358e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00918337, Final residual = 2.48306e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00254711, Final residual = 1.55056e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00282572, Final residual = 1.37624e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00302166, Final residual = 1.63326e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00302168, Final residual = 1.63459e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00223525, Final residual = 1.36495e-07, No Iterations 1 +min/max(T) = 621.459, 863.782 +GAMG: Solving for p, Initial residual = 0.0357621, Final residual = 0.000373652, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.97667e-06, global = 1.94026e-06, cumulative = 0.000396938 +GAMG: Solving for p, Initial residual = 0.00035265, Final residual = 6.179e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.94369e-06, global = 1.94363e-06, cumulative = 0.000398881 +smoothSolver: Solving for epsilon, Initial residual = 0.00116484, Final residual = 2.06845e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00371266, Final residual = 6.34387e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103931 s +other Time = 1e-06 s +rho Equations = 0.000288 s +U Equations = 0.001636 s +Y Equations = 0.00292666 s +E Equations = 0.000699 s +p Equations = 0.002907 s +calculate parcels = 18.3077 s +chemistry correctThermo = 0.002853 s +turbulence correct = 0.00131 s +combustion correct(in Y) = 0.0910343 s +percentage of chemistry = 87.5911 % +percentage of rho/U/Y/E = 5.33976 % +========Time details of each equation======= +rhoEqn Time = 0.00049 s +rhoEqn assamble = 0.000396 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001633 s +UEqn assamble = 0.001023 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00061 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002028 s +YEqn assamble = 0.000756 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000118 s +YEqn correct boundary = 0 s +EEqn Time = 0.000512 s +EEqn assamble = 0.000373 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000139 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 39.96 s ClockTime = 40 s +Courant Number mean: 0.000287251 max: 0.0194379 +Time = 0.00062 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 52 new parcels + +Cloud: sprayCloud + Current number of parcels = 10190 + Current mass in system = 9.91699e-10 + Linear momentum = (3.00886e-11 -9.2347e-09 0) + |Linear momentum| = 9.23475e-09 + Linear kinetic energy = 4.56265e-08 + model1: + number of parcels added = 10198 + mass introduced = 1.00911e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.137, 524.536 + Mass transfer phase change = 1.74101e-11 + D10, D32, Dmax (mu) = 48.4031, 79.6056, 149.429 + Liquid penetration 95% mass (m) = 0.00494306 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00401994, Final residual = 6.53516e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00904432, Final residual = 2.47411e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00254317, Final residual = 1.5422e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00281644, Final residual = 1.37988e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00301102, Final residual = 1.63342e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00301104, Final residual = 1.63476e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00222679, Final residual = 1.36691e-07, No Iterations 1 +min/max(T) = 621.283, 864.564 +GAMG: Solving for p, Initial residual = 0.0348752, Final residual = 0.000372198, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.99215e-06, global = 1.95153e-06, cumulative = 0.000400833 +GAMG: Solving for p, Initial residual = 0.00035573, Final residual = 5.03625e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.95722e-06, global = 1.95716e-06, cumulative = 0.00040279 +smoothSolver: Solving for epsilon, Initial residual = 0.00116501, Final residual = 2.06754e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00369695, Final residual = 6.30951e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.077648 s +other Time = 0 s +rho Equations = 0.000205 s +U Equations = 0.001098 s +Y Equations = 0.00233836 s +E Equations = 0.000523 s +p Equations = 0.003165 s +calculate parcels = 18.4817 s +chemistry correctThermo = 0.002015 s +turbulence correct = 0.001436 s +combustion correct(in Y) = 0.0666516 s +percentage of chemistry = 85.8382 % +percentage of rho/U/Y/E = 5.36312 % +========Time details of each equation======= +rhoEqn Time = 0.000417 s +rhoEqn assamble = 0.000335 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001097 s +UEqn assamble = 0.000695 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000402 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001711 s +YEqn assamble = 0.000605 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000142 s +YEqn correct boundary = 0 s +EEqn Time = 0.000391 s +EEqn assamble = 0.000295 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 40.21 s ClockTime = 41 s +Courant Number mean: 0.000288847 max: 0.01943 +Time = 0.0006225 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 45 new parcels + +Cloud: sprayCloud + Current number of parcels = 10235 + Current mass in system = 9.94877e-10 + Linear momentum = (3.00943e-11 -9.25089e-09 0) + |Linear momentum| = 9.25094e-09 + Linear kinetic energy = 4.56359e-08 + model1: + number of parcels added = 10243 + mass introduced = 1.01246e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.131, 526.449 + Mass transfer phase change = 1.7581e-11 + D10, D32, Dmax (mu) = 48.4222, 79.6512, 149.434 + Liquid penetration 95% mass (m) = 0.00496206 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00388017, Final residual = 6.39101e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00892213, Final residual = 2.49724e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00253213, Final residual = 1.53589e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0028074, Final residual = 1.3744e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00300183, Final residual = 1.63317e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00300185, Final residual = 1.6345e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00221472, Final residual = 1.35893e-07, No Iterations 1 +min/max(T) = 621.113, 865.352 +GAMG: Solving for p, Initial residual = 0.0342781, Final residual = 0.000349041, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.00432e-06, global = 1.96402e-06, cumulative = 0.000404754 +GAMG: Solving for p, Initial residual = 0.000334504, Final residual = 4.88177e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.96986e-06, global = 1.9698e-06, cumulative = 0.000406724 +smoothSolver: Solving for epsilon, Initial residual = 0.00116512, Final residual = 2.0671e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00368145, Final residual = 6.27661e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.098135 s +other Time = 0 s +rho Equations = 0.000238 s +U Equations = 0.001465 s +Y Equations = 0.0033684 s +E Equations = 0.000724 s +p Equations = 0.002929 s +calculate parcels = 18.6707 s +chemistry correctThermo = 0.002826 s +turbulence correct = 0.001399 s +combustion correct(in Y) = 0.0849286 s +percentage of chemistry = 86.5426 % +percentage of rho/U/Y/E = 5.90554 % +========Time details of each equation======= +rhoEqn Time = 0.000439 s +rhoEqn assamble = 0.000349 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001463 s +UEqn assamble = 0.000947 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000516 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002457 s +YEqn assamble = 0.000938 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000118 s +YEqn correct boundary = 0 s +EEqn Time = 0.000524 s +EEqn assamble = 0.000405 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000119 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 40.5 s ClockTime = 41 s +Courant Number mean: 0.000290371 max: 0.0194319 +Time = 0.000625 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 56 new parcels + +Cloud: sprayCloud + Current number of parcels = 10291 + Current mass in system = 9.98837e-10 + Linear momentum = (3.01759e-11 -9.2753e-09 0) + |Linear momentum| = 9.27534e-09 + Linear kinetic energy = 4.5689e-08 + model1: + number of parcels added = 10299 + mass introduced = 1.01659e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.126, 528.077 + Mass transfer phase change = 1.77531e-11 + D10, D32, Dmax (mu) = 48.4559, 79.6833, 149.558 + Liquid penetration 95% mass (m) = 0.00497906 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00372645, Final residual = 6.21822e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0088325, Final residual = 2.49823e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00251583, Final residual = 1.5259e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0027983, Final residual = 1.37584e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00299176, Final residual = 1.63298e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00299178, Final residual = 1.63432e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00220547, Final residual = 1.36375e-07, No Iterations 1 +min/max(T) = 620.941, 866.148 +GAMG: Solving for p, Initial residual = 0.0339942, Final residual = 0.000363463, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.02004e-06, global = 1.97728e-06, cumulative = 0.000408701 +GAMG: Solving for p, Initial residual = 0.000349454, Final residual = 6.0481e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.98329e-06, global = 1.98323e-06, cumulative = 0.000410684 +smoothSolver: Solving for epsilon, Initial residual = 0.00116435, Final residual = 2.06523e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00366625, Final residual = 6.24183e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.093423 s +other Time = 1e-06 s +rho Equations = 0.000202 s +U Equations = 0.001294 s +Y Equations = 0.00238307 s +E Equations = 0.000554 s +p Equations = 0.002031 s +calculate parcels = 18.8528 s +chemistry correctThermo = 0.001967 s +turbulence correct = 0.000904 s +combustion correct(in Y) = 0.0838849 s +percentage of chemistry = 89.7905 % +percentage of rho/U/Y/E = 4.74516 % +========Time details of each equation======= +rhoEqn Time = 0.000332 s +rhoEqn assamble = 0.000265 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001292 s +UEqn assamble = 0.000825 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000467 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001614 s +YEqn assamble = 0.000582 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000126 s +YEqn correct boundary = 0 s +EEqn Time = 0.000404 s +EEqn assamble = 0.000305 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 40.78 s ClockTime = 41 s +Courant Number mean: 0.000291882 max: 0.0194247 +Time = 0.0006275 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 52 new parcels + +Cloud: sprayCloud + Current number of parcels = 10343 + Current mass in system = 1.0025e-09 + Linear momentum = (3.01121e-11 -9.29645e-09 0) + |Linear momentum| = 9.2965e-09 + Linear kinetic energy = 4.57242e-08 + model1: + number of parcels added = 10351 + mass introduced = 1.02043e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.149, 529.452 + Mass transfer phase change = 1.79262e-11 + D10, D32, Dmax (mu) = 48.4861, 79.7193, 149.482 + Liquid penetration 95% mass (m) = 0.00499621 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00352701, Final residual = 6.06438e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00885164, Final residual = 2.49071e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00250326, Final residual = 1.51628e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00278926, Final residual = 1.37325e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00298269, Final residual = 1.63278e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0029827, Final residual = 1.63411e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0021945, Final residual = 1.36026e-07, No Iterations 1 +min/max(T) = 620.778, 866.95 +GAMG: Solving for p, Initial residual = 0.033207, Final residual = 0.000313982, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.02798e-06, global = 1.98974e-06, cumulative = 0.000412674 +GAMG: Solving for p, Initial residual = 0.000300961, Final residual = 3.54411e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.9956e-06, global = 1.99557e-06, cumulative = 0.00041467 +smoothSolver: Solving for epsilon, Initial residual = 0.00116366, Final residual = 2.06319e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00365044, Final residual = 6.20693e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097599 s +other Time = 1e-06 s +rho Equations = 0.000175 s +U Equations = 0.001107 s +Y Equations = 0.00243017 s +E Equations = 0.0006 s +p Equations = 0.002188 s +calculate parcels = 19.0183 s +chemistry correctThermo = 0.00281 s +turbulence correct = 0.001017 s +combustion correct(in Y) = 0.0870748 s +percentage of chemistry = 89.2169 % +percentage of rho/U/Y/E = 4.41825 % +========Time details of each equation======= +rhoEqn Time = 0.000318 s +rhoEqn assamble = 0.000252 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001107 s +UEqn assamble = 0.000673 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000434 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001779 s +YEqn assamble = 0.000664 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000187 s +YEqn correct boundary = 0 s +EEqn Time = 0.000442 s +EEqn assamble = 0.000327 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 41.04 s ClockTime = 41 s +Courant Number mean: 0.000293326 max: 0.0194253 +Time = 0.00063 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 10392 + Current mass in system = 1.00595e-09 + Linear momentum = (2.95452e-11 -9.31527e-09 0) + |Linear momentum| = 9.31532e-09 + Linear kinetic energy = 4.57475e-08 + model1: + number of parcels added = 10400 + mass introduced = 1.02405e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.159, 529.32 + Mass transfer phase change = 1.81003e-11 + D10, D32, Dmax (mu) = 48.4954, 79.7632, 149.567 + Liquid penetration 95% mass (m) = 0.00501356 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0035859, Final residual = 6.16686e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00910934, Final residual = 2.52457e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00247658, Final residual = 1.53184e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00277956, Final residual = 1.37718e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00297414, Final residual = 1.63177e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00297416, Final residual = 1.63313e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00218093, Final residual = 1.34879e-07, No Iterations 1 +min/max(T) = 620.605, 867.758 +GAMG: Solving for p, Initial residual = 0.0336364, Final residual = 0.000453946, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.04974e-06, global = 1.99724e-06, cumulative = 0.000416667 +GAMG: Solving for p, Initial residual = 0.000439551, Final residual = 5.56302e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.00638e-06, global = 2.00631e-06, cumulative = 0.000418673 +smoothSolver: Solving for epsilon, Initial residual = 0.00116319, Final residual = 2.0617e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00363399, Final residual = 6.17157e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095196 s +other Time = 0 s +rho Equations = 0.000175 s +U Equations = 0.001151 s +Y Equations = 0.00201514 s +E Equations = 0.000484 s +p Equations = 0.001852 s +calculate parcels = 19.1857 s +chemistry correctThermo = 0.001988 s +turbulence correct = 0.000808 s +combustion correct(in Y) = 0.0865239 s +percentage of chemistry = 90.8902 % +percentage of rho/U/Y/E = 4.01817 % +========Time details of each equation======= +rhoEqn Time = 0.000316 s +rhoEqn assamble = 0.000247 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001151 s +UEqn assamble = 0.000706 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000445 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001328 s +YEqn assamble = 0.000522 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 6.3e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000364 s +EEqn assamble = 0.000272 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 41.3 s ClockTime = 42 s +Courant Number mean: 0.000294693 max: 0.0194589 +Time = 0.0006325 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 53 new parcels + +Cloud: sprayCloud + Current number of parcels = 10445 + Current mass in system = 1.00968e-09 + Linear momentum = (2.96121e-11 -9.33732e-09 0) + |Linear momentum| = 9.33736e-09 + Linear kinetic energy = 4.57886e-08 + model1: + number of parcels added = 10453 + mass introduced = 1.02796e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.134, 528.274 + Mass transfer phase change = 1.82751e-11 + D10, D32, Dmax (mu) = 48.5222, 79.7996, 149.477 + Liquid penetration 95% mass (m) = 0.00503138 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00385226, Final residual = 6.61677e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00955987, Final residual = 2.63435e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00246508, Final residual = 1.54437e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00276864, Final residual = 1.37299e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00296575, Final residual = 1.63376e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00296576, Final residual = 1.63512e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00216761, Final residual = 1.34151e-07, No Iterations 1 +min/max(T) = 620.438, 868.573 +GAMG: Solving for p, Initial residual = 0.0328661, Final residual = 0.000355879, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.05205e-06, global = 2.00867e-06, cumulative = 0.000420682 +GAMG: Solving for p, Initial residual = 0.000340999, Final residual = 3.83454e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.01476e-06, global = 2.01471e-06, cumulative = 0.000422696 +smoothSolver: Solving for epsilon, Initial residual = 0.00116286, Final residual = 2.06009e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0036175, Final residual = 6.13818e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.096641 s +other Time = 0 s +rho Equations = 0.000168 s +U Equations = 0.001178 s +Y Equations = 0.0023597 s +E Equations = 0.00059 s +p Equations = 0.002334 s +calculate parcels = 19.3629 s +chemistry correctThermo = 0.002802 s +turbulence correct = 0.000981 s +combustion correct(in Y) = 0.0860363 s +percentage of chemistry = 89.0267 % +percentage of rho/U/Y/E = 4.44501 % +========Time details of each equation======= +rhoEqn Time = 0.000315 s +rhoEqn assamble = 0.000246 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001176 s +UEqn assamble = 0.000725 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000451 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001641 s +YEqn assamble = 0.000625 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000141 s +YEqn correct boundary = 0 s +EEqn Time = 0.000438 s +EEqn assamble = 0.000324 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 41.58 s ClockTime = 42 s +Courant Number mean: 0.000295939 max: 0.0194423 +Time = 0.000635 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 10493 + Current mass in system = 1.01306e-09 + Linear momentum = (2.92327e-11 -9.35549e-09 0) + |Linear momentum| = 9.35554e-09 + Linear kinetic energy = 4.58094e-08 + model1: + number of parcels added = 10501 + mass introduced = 1.03151e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.149, 527.125 + Mass transfer phase change = 1.84506e-11 + D10, D32, Dmax (mu) = 48.5226, 79.8383, 149.462 + Liquid penetration 95% mass (m) = 0.00504875 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00376299, Final residual = 6.54527e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0100819, Final residual = 2.78312e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00245417, Final residual = 1.53953e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0027576, Final residual = 1.36662e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00295714, Final residual = 1.63503e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00295716, Final residual = 1.6364e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00215577, Final residual = 1.33993e-07, No Iterations 1 +min/max(T) = 620.271, 869.396 +GAMG: Solving for p, Initial residual = 0.0322494, Final residual = 0.000358675, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.06441e-06, global = 2.01446e-06, cumulative = 0.000424711 +GAMG: Solving for p, Initial residual = 0.00034542, Final residual = 3.31665e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.02296e-06, global = 2.02292e-06, cumulative = 0.000426734 +smoothSolver: Solving for epsilon, Initial residual = 0.00116216, Final residual = 2.05788e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00360182, Final residual = 6.10552e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.084132 s +other Time = 0 s +rho Equations = 0.000179 s +U Equations = 0.001143 s +Y Equations = 0.00235189 s +E Equations = 0.000616 s +p Equations = 0.002226 s +calculate parcels = 19.5424 s +chemistry correctThermo = 0.002747 s +turbulence correct = 0.000959 s +combustion correct(in Y) = 0.0736991 s +percentage of chemistry = 87.5994 % +percentage of rho/U/Y/E = 5.099 % +========Time details of each equation======= +rhoEqn Time = 0.000322 s +rhoEqn assamble = 0.000254 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001143 s +UEqn assamble = 0.000702 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000441 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001688 s +YEqn assamble = 0.000632 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000162 s +YEqn correct boundary = 0 s +EEqn Time = 0.000464 s +EEqn assamble = 0.00035 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 41.84 s ClockTime = 42 s +Courant Number mean: 0.00029716 max: 0.0194051 +Time = 0.0006375 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 42 new parcels + +Cloud: sprayCloud + Current number of parcels = 10535 + Current mass in system = 1.01598e-09 + Linear momentum = (2.95259e-11 -9.36893e-09 0) + |Linear momentum| = 9.36898e-09 + Linear kinetic energy = 4.58054e-08 + model1: + number of parcels added = 10543 + mass introduced = 1.03461e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.147, 525.873 + Mass transfer phase change = 1.86268e-11 + D10, D32, Dmax (mu) = 48.5447, 79.8931, 149.702 + Liquid penetration 95% mass (m) = 0.00506716 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00361969, Final residual = 6.24004e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0105878, Final residual = 2.9055e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00243716, Final residual = 1.54739e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00274694, Final residual = 1.35876e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00294934, Final residual = 1.63611e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00294935, Final residual = 1.63747e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00214073, Final residual = 1.33087e-07, No Iterations 1 +min/max(T) = 620.114, 870.227 +GAMG: Solving for p, Initial residual = 0.031382, Final residual = 0.000269944, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.06192e-06, global = 2.02354e-06, cumulative = 0.000428757 +GAMG: Solving for p, Initial residual = 0.00026012, Final residual = 2.43314e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.03028e-06, global = 2.03025e-06, cumulative = 0.000430788 +smoothSolver: Solving for epsilon, Initial residual = 0.00116128, Final residual = 2.05559e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00358588, Final residual = 6.07303e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.091086 s +other Time = 1e-06 s +rho Equations = 0.000167 s +U Equations = 0.001101 s +Y Equations = 0.0027754 s +E Equations = 0.000692 s +p Equations = 0.002333 s +calculate parcels = 19.7131 s +chemistry correctThermo = 0.002792 s +turbulence correct = 0.001014 s +combustion correct(in Y) = 0.0800156 s +percentage of chemistry = 87.8462 % +percentage of rho/U/Y/E = 5.19882 % +========Time details of each equation======= +rhoEqn Time = 0.000325 s +rhoEqn assamble = 0.000251 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001101 s +UEqn assamble = 0.000677 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000424 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002077 s +YEqn assamble = 0.000807 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000208 s +YEqn correct boundary = 0 s +EEqn Time = 0.000495 s +EEqn assamble = 0.000372 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000123 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 42.1 s ClockTime = 43 s +Courant Number mean: 0.000298416 max: 0.0193885 +Time = 0.00064 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 45 new parcels + +Cloud: sprayCloud + Current number of parcels = 10580 + Current mass in system = 1.01912e-09 + Linear momentum = (2.9513e-11 -9.38474e-09 0) + |Linear momentum| = 9.38478e-09 + Linear kinetic energy = 4.58144e-08 + model1: + number of parcels added = 10588 + mass introduced = 1.03792e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.135, 524.53 + Mass transfer phase change = 1.88036e-11 + D10, D32, Dmax (mu) = 48.5659, 79.925, 149.825 + Liquid penetration 95% mass (m) = 0.00508553 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00372749, Final residual = 6.37693e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0110821, Final residual = 3.00826e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00242124, Final residual = 1.56498e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00273772, Final residual = 1.35268e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00294235, Final residual = 1.63861e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00294236, Final residual = 1.63996e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00212831, Final residual = 1.32529e-07, No Iterations 1 +min/max(T) = 619.962, 871.065 +GAMG: Solving for p, Initial residual = 0.0306129, Final residual = 0.000270456, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.07303e-06, global = 2.03111e-06, cumulative = 0.000432819 +GAMG: Solving for p, Initial residual = 0.000261825, Final residual = 2.88719e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.03895e-06, global = 2.03892e-06, cumulative = 0.000434858 +smoothSolver: Solving for epsilon, Initial residual = 0.00116007, Final residual = 2.05268e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00356961, Final residual = 6.03989e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.072412 s +other Time = 0 s +rho Equations = 0.000173 s +U Equations = 0.001008 s +Y Equations = 0.00262742 s +E Equations = 0.000528 s +p Equations = 0.001964 s +calculate parcels = 19.8937 s +chemistry correctThermo = 0.002005 s +turbulence correct = 0.000873 s +combustion correct(in Y) = 0.0630466 s +percentage of chemistry = 87.0665 % +percentage of rho/U/Y/E = 5.98853 % +========Time details of each equation======= +rhoEqn Time = 0.000301 s +rhoEqn assamble = 0.000244 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001007 s +UEqn assamble = 0.000635 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000372 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002046 s +YEqn assamble = 0.000707 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000255 s +YEqn correct boundary = 0 s +EEqn Time = 0.000389 s +EEqn assamble = 0.000293 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 42.35 s ClockTime = 43 s +Courant Number mean: 0.000299736 max: 0.0193615 +Time = 0.0006425 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 57 new parcels + +Cloud: sprayCloud + Current number of parcels = 10637 + Current mass in system = 1.02313e-09 + Linear momentum = (2.92093e-11 -9.40989e-09 0) + |Linear momentum| = 9.40993e-09 + Linear kinetic energy = 4.58746e-08 + model1: + number of parcels added = 10645 + mass introduced = 1.04211e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.135, 523.795 + Mass transfer phase change = 1.89813e-11 + D10, D32, Dmax (mu) = 48.5884, 79.9807, 149.735 + Liquid penetration 95% mass (m) = 0.00510209 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00385632, Final residual = 6.68316e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0116264, Final residual = 3.11323e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00241849, Final residual = 1.56463e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00272808, Final residual = 1.35049e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00293451, Final residual = 1.63961e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00293452, Final residual = 1.64096e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00211722, Final residual = 1.32173e-07, No Iterations 1 +min/max(T) = 619.805, 871.909 +GAMG: Solving for p, Initial residual = 0.0301061, Final residual = 0.000293983, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.08185e-06, global = 2.03987e-06, cumulative = 0.000436898 +GAMG: Solving for p, Initial residual = 0.000283885, Final residual = 3.05698e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.04783e-06, global = 2.04779e-06, cumulative = 0.000438945 +smoothSolver: Solving for epsilon, Initial residual = 0.00115849, Final residual = 2.04932e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00355313, Final residual = 6.00585e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.068469 s +other Time = 1e-06 s +rho Equations = 0.000275 s +U Equations = 0.001345 s +Y Equations = 0.00204717 s +E Equations = 0.000512 s +p Equations = 0.001878 s +calculate parcels = 20.0287 s +chemistry correctThermo = 0.001876 s +turbulence correct = 0.000823 s +combustion correct(in Y) = 0.0595178 s +percentage of chemistry = 86.9267 % +percentage of rho/U/Y/E = 6.10374 % +========Time details of each equation======= +rhoEqn Time = 0.000396 s +rhoEqn assamble = 0.000304 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001344 s +UEqn assamble = 0.000932 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000412 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.0014 s +YEqn assamble = 0.00054 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 7.7e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000393 s +EEqn assamble = 0.000295 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 42.56 s ClockTime = 43 s +Courant Number mean: 0.000301182 max: 0.0193546 +Time = 0.000645 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 10688 + Current mass in system = 1.02671e-09 + Linear momentum = (2.92945e-11 -9.43047e-09 0) + |Linear momentum| = 9.43052e-09 + Linear kinetic energy = 4.59103e-08 + model1: + number of parcels added = 10696 + mass introduced = 1.04587e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.137, 525.777 + Mass transfer phase change = 1.91598e-11 + D10, D32, Dmax (mu) = 48.3828, 79.9939, 149.617 + Liquid penetration 95% mass (m) = 0.00511844 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00407242, Final residual = 7.07049e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0122041, Final residual = 3.21504e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00240281, Final residual = 1.56892e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00271959, Final residual = 1.34708e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00292788, Final residual = 1.64071e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00292789, Final residual = 1.64206e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00210883, Final residual = 1.3249e-07, No Iterations 1 +min/max(T) = 619.661, 872.76 +GAMG: Solving for p, Initial residual = 0.0291782, Final residual = 0.000283525, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.09135e-06, global = 2.04814e-06, cumulative = 0.000440993 +GAMG: Solving for p, Initial residual = 0.000273304, Final residual = 3.56211e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.0578e-06, global = 2.05776e-06, cumulative = 0.000443051 +smoothSolver: Solving for epsilon, Initial residual = 0.00115675, Final residual = 2.04533e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00353572, Final residual = 5.97045e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.106083 s +other Time = 0 s +rho Equations = 0.000172 s +U Equations = 0.001089 s +Y Equations = 0.00241984 s +E Equations = 0.000505 s +p Equations = 0.00325 s +calculate parcels = 20.2096 s +chemistry correctThermo = 0.002027 s +turbulence correct = 0.001669 s +combustion correct(in Y) = 0.0947092 s +percentage of chemistry = 89.2784 % +percentage of rho/U/Y/E = 3.94582 % +========Time details of each equation======= +rhoEqn Time = 0.00045 s +rhoEqn assamble = 0.00034 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.00011 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001088 s +UEqn assamble = 0.000669 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000419 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00174 s +YEqn assamble = 0.000654 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00016 s +YEqn correct boundary = 0 s +EEqn Time = 0.000382 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 42.84 s ClockTime = 43 s +Courant Number mean: 0.000302812 max: 0.0193453 +Time = 0.0006475 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 10736 + Current mass in system = 1.03007e-09 + Linear momentum = (2.962e-11 -9.44878e-09 0) + |Linear momentum| = 9.44883e-09 + Linear kinetic energy = 4.59341e-08 + model1: + number of parcels added = 10744 + mass introduced = 1.04941e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.133, 527.5 + Mass transfer phase change = 1.93392e-11 + D10, D32, Dmax (mu) = 48.4013, 80.0375, 149.487 + Liquid penetration 95% mass (m) = 0.00513528 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00423481, Final residual = 7.42097e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0128106, Final residual = 3.30829e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00238223, Final residual = 1.56715e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00271036, Final residual = 1.34321e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00292085, Final residual = 1.641e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00292087, Final residual = 1.64235e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0020957, Final residual = 1.31747e-07, No Iterations 1 +min/max(T) = 619.523, 873.619 +GAMG: Solving for p, Initial residual = 0.0283297, Final residual = 0.000290866, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.10726e-06, global = 2.0582e-06, cumulative = 0.000445109 +GAMG: Solving for p, Initial residual = 0.000281637, Final residual = 3.76936e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.06688e-06, global = 2.06683e-06, cumulative = 0.000447176 +smoothSolver: Solving for epsilon, Initial residual = 0.00115559, Final residual = 2.04219e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00351589, Final residual = 5.93162e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.07587 s +other Time = 0 s +rho Equations = 0.000168 s +U Equations = 0.00115 s +Y Equations = 0.00198391 s +E Equations = 0.000519 s +p Equations = 0.001796 s +calculate parcels = 20.3877 s +chemistry correctThermo = 0.001982 s +turbulence correct = 0.000874 s +combustion correct(in Y) = 0.0672111 s +percentage of chemistry = 88.5872 % +percentage of rho/U/Y/E = 5.03612 % +========Time details of each equation======= +rhoEqn Time = 0.000303 s +rhoEqn assamble = 0.000238 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001149 s +UEqn assamble = 0.000737 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000412 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001417 s +YEqn assamble = 0.000524 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000128 s +YEqn correct boundary = 0 s +EEqn Time = 0.0004 s +EEqn assamble = 0.000304 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 43.1 s ClockTime = 44 s +Courant Number mean: 0.000304553 max: 0.0193298 +Time = 0.00065 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 10785 + Current mass in system = 1.03351e-09 + Linear momentum = (2.93184e-11 -9.46784e-09 0) + |Linear momentum| = 9.46789e-09 + Linear kinetic energy = 4.59625e-08 + model1: + number of parcels added = 10793 + mass introduced = 1.05302e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.139, 528.589 + Mass transfer phase change = 1.95194e-11 + D10, D32, Dmax (mu) = 48.3935, 80.0625, 149.492 + Liquid penetration 95% mass (m) = 0.00515216 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00431466, Final residual = 7.55357e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0134477, Final residual = 3.44042e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00237066, Final residual = 1.55487e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00270218, Final residual = 1.33657e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00291407, Final residual = 1.64017e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00291408, Final residual = 1.64152e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00208528, Final residual = 1.30649e-07, No Iterations 1 +min/max(T) = 619.39, 874.485 +GAMG: Solving for p, Initial residual = 0.0276266, Final residual = 0.000260052, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.11348e-06, global = 2.06977e-06, cumulative = 0.000449246 +GAMG: Solving for p, Initial residual = 0.000250949, Final residual = 2.61068e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.07729e-06, global = 2.07725e-06, cumulative = 0.000451323 +smoothSolver: Solving for epsilon, Initial residual = 0.00115409, Final residual = 2.03863e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00349394, Final residual = 5.88936e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.07668 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001133 s +Y Equations = 0.00225803 s +E Equations = 0.000507 s +p Equations = 0.001926 s +calculate parcels = 20.5492 s +chemistry correctThermo = 0.002238 s +turbulence correct = 0.00096 s +combustion correct(in Y) = 0.067277 s +percentage of chemistry = 87.7373 % +percentage of rho/U/Y/E = 5.31433 % +========Time details of each equation======= +rhoEqn Time = 0.0003 s +rhoEqn assamble = 0.000237 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001132 s +UEqn assamble = 0.000693 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000439 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001603 s +YEqn assamble = 0.000606 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000175 s +YEqn correct boundary = 0 s +EEqn Time = 0.000382 s +EEqn assamble = 0.000286 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 43.34 s ClockTime = 44 s +Courant Number mean: 0.000306467 max: 0.0193042 +Time = 0.0006525 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 61 new parcels + +Cloud: sprayCloud + Current number of parcels = 10846 + Current mass in system = 1.03782e-09 + Linear momentum = (2.84785e-11 -9.49639e-09 0) + |Linear momentum| = 9.49643e-09 + Linear kinetic energy = 4.60427e-08 + model1: + number of parcels added = 10854 + mass introduced = 1.05752e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.135, 528 + Mass transfer phase change = 1.97004e-11 + D10, D32, Dmax (mu) = 48.4127, 80.1036, 149.497 + Liquid penetration 95% mass (m) = 0.00516844 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00417268, Final residual = 7.28642e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0140522, Final residual = 3.59094e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00241633, Final residual = 1.67219e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00269371, Final residual = 1.3423e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00290776, Final residual = 1.63826e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00290778, Final residual = 1.63961e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00207926, Final residual = 1.30416e-07, No Iterations 1 +min/max(T) = 619.272, 875.36 +GAMG: Solving for p, Initial residual = 0.0273085, Final residual = 0.000315178, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.12574e-06, global = 2.07829e-06, cumulative = 0.000453402 +GAMG: Solving for p, Initial residual = 0.000306347, Final residual = 2.12184e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.08682e-06, global = 2.08679e-06, cumulative = 0.000455488 +smoothSolver: Solving for epsilon, Initial residual = 0.00115216, Final residual = 2.03431e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00346975, Final residual = 5.84196e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.098344 s +other Time = 0 s +rho Equations = 0.00017 s +U Equations = 0.001188 s +Y Equations = 0.00244324 s +E Equations = 0.000599 s +p Equations = 0.002208 s +calculate parcels = 20.7307 s +chemistry correctThermo = 0.00275 s +turbulence correct = 0.001161 s +combustion correct(in Y) = 0.0876248 s +percentage of chemistry = 89.1003 % +percentage of rho/U/Y/E = 4.47433 % +========Time details of each equation======= +rhoEqn Time = 0.000315 s +rhoEqn assamble = 0.00025 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001187 s +UEqn assamble = 0.000703 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000484 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001768 s +YEqn assamble = 0.000665 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000184 s +YEqn correct boundary = 0 s +EEqn Time = 0.000444 s +EEqn assamble = 0.000331 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 43.62 s ClockTime = 44 s +Courant Number mean: 0.0003086 max: 0.019337 +Time = 0.000655 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 10896 + Current mass in system = 1.04134e-09 + Linear momentum = (2.94896e-11 -9.51643e-09 0) + |Linear momentum| = 9.51647e-09 + Linear kinetic energy = 4.60774e-08 + model1: + number of parcels added = 10904 + mass introduced = 1.06122e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.142, 527.348 + Mass transfer phase change = 1.98822e-11 + D10, D32, Dmax (mu) = 48.4053, 80.1235, 149.502 + Liquid penetration 95% mass (m) = 0.00518398 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00426412, Final residual = 7.32622e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0145974, Final residual = 3.70653e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00242103, Final residual = 1.70049e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00268442, Final residual = 1.34275e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00290149, Final residual = 1.63748e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00290151, Final residual = 1.63882e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00207072, Final residual = 1.30968e-07, No Iterations 1 +min/max(T) = 619.17, 876.242 +GAMG: Solving for p, Initial residual = 0.0261414, Final residual = 0.000240038, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.1294e-06, global = 2.08702e-06, cumulative = 0.000457575 +GAMG: Solving for p, Initial residual = 0.000232701, Final residual = 1.78039e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.09454e-06, global = 2.09451e-06, cumulative = 0.00045967 +smoothSolver: Solving for epsilon, Initial residual = 0.00115069, Final residual = 2.03067e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00344637, Final residual = 5.79771e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.084205 s +other Time = 1e-06 s +rho Equations = 0.000243 s +U Equations = 0.001612 s +Y Equations = 0.00217941 s +E Equations = 0.000505 s +p Equations = 0.00226 s +calculate parcels = 20.8945 s +chemistry correctThermo = 0.002497 s +turbulence correct = 0.001067 s +combustion correct(in Y) = 0.0736026 s +percentage of chemistry = 87.4088 % +percentage of rho/U/Y/E = 5.3909 % +========Time details of each equation======= +rhoEqn Time = 0.000387 s +rhoEqn assamble = 0.000298 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001609 s +UEqn assamble = 0.000895 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000714 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001338 s +YEqn assamble = 0.00055 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9e-06 s +YEqn correct boundary = 0 s +EEqn Time = 0.000383 s +EEqn assamble = 0.000288 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 43.87 s ClockTime = 44 s +Courant Number mean: 0.000310978 max: 0.0193236 +Time = 0.0006575 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 52 new parcels + +Cloud: sprayCloud + Current number of parcels = 10948 + Current mass in system = 1.04501e-09 + Linear momentum = (2.95766e-11 -9.53813e-09 0) + |Linear momentum| = 9.53818e-09 + Linear kinetic energy = 4.61214e-08 + model1: + number of parcels added = 10956 + mass introduced = 1.06507e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.137, 526.599 + Mass transfer phase change = 2.00644e-11 + D10, D32, Dmax (mu) = 48.4248, 80.1695, 149.705 + Liquid penetration 95% mass (m) = 0.00520183 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00397567, Final residual = 6.92367e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0151291, Final residual = 3.84543e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00241197, Final residual = 1.68913e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00267494, Final residual = 1.34073e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00289555, Final residual = 1.63597e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00289557, Final residual = 1.63731e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00205889, Final residual = 1.31827e-07, No Iterations 1 +min/max(T) = 619.09, 877.133 +GAMG: Solving for p, Initial residual = 0.025347, Final residual = 0.000223132, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.13568e-06, global = 2.09295e-06, cumulative = 0.000461763 +GAMG: Solving for p, Initial residual = 0.000214464, Final residual = 1.55942e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.10102e-06, global = 2.10099e-06, cumulative = 0.000463864 +smoothSolver: Solving for epsilon, Initial residual = 0.00114944, Final residual = 2.02754e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0034239, Final residual = 5.75579e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.087064 s +other Time = 0 s +rho Equations = 0.00014 s +U Equations = 0.000968 s +Y Equations = 0.00233934 s +E Equations = 0.000609 s +p Equations = 0.0023 s +calculate parcels = 21.0527 s +chemistry correctThermo = 0.002771 s +turbulence correct = 0.000967 s +combustion correct(in Y) = 0.0767967 s +percentage of chemistry = 88.2071 % +percentage of rho/U/Y/E = 4.65903 % +========Time details of each equation======= +rhoEqn Time = 0.000291 s +rhoEqn assamble = 0.000231 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000966 s +UEqn assamble = 0.000578 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000388 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001784 s +YEqn assamble = 0.000652 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000218 s +YEqn correct boundary = 0 s +EEqn Time = 0.000453 s +EEqn assamble = 0.00034 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 44.11 s ClockTime = 45 s +Courant Number mean: 0.000313681 max: 0.0193051 +Time = 0.00066 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 54 new parcels + +Cloud: sprayCloud + Current number of parcels = 11002 + Current mass in system = 1.04883e-09 + Linear momentum = (2.93661e-11 -9.56148e-09 0) + |Linear momentum| = 9.56152e-09 + Linear kinetic energy = 4.61749e-08 + model1: + number of parcels added = 11010 + mass introduced = 1.06908e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.135, 525.755 + Mass transfer phase change = 2.02472e-11 + D10, D32, Dmax (mu) = 48.4425, 80.2091, 149.59 + Liquid penetration 95% mass (m) = 0.00521725 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00377547, Final residual = 6.56423e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0156047, Final residual = 3.97455e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00239282, Final residual = 1.66667e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00266556, Final residual = 1.33796e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00288976, Final residual = 1.63436e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00288977, Final residual = 1.63569e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00204201, Final residual = 1.30982e-07, No Iterations 1 +min/max(T) = 619.019, 878.032 +GAMG: Solving for p, Initial residual = 0.0249161, Final residual = 0.000223495, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.14137e-06, global = 2.10062e-06, cumulative = 0.000465964 +GAMG: Solving for p, Initial residual = 0.000217772, Final residual = 2.04853e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.10691e-06, global = 2.10687e-06, cumulative = 0.000468071 +smoothSolver: Solving for epsilon, Initial residual = 0.00114764, Final residual = 2.02408e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00340196, Final residual = 5.71509e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095678 s +other Time = 0 s +rho Equations = 0.000164 s +U Equations = 0.001154 s +Y Equations = 0.00239128 s +E Equations = 0.000615 s +p Equations = 0.002258 s +calculate parcels = 21.235 s +chemistry correctThermo = 0.002783 s +turbulence correct = 0.000994 s +combustion correct(in Y) = 0.0851207 s +percentage of chemistry = 88.9658 % +percentage of rho/U/Y/E = 4.51962 % +========Time details of each equation======= +rhoEqn Time = 0.000305 s +rhoEqn assamble = 0.000242 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001152 s +UEqn assamble = 0.000715 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000437 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001765 s +YEqn assamble = 0.000641 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000209 s +YEqn correct boundary = 0 s +EEqn Time = 0.000463 s +EEqn assamble = 0.00034 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000123 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 44.39 s ClockTime = 45 s +Courant Number mean: 0.000316954 max: 0.0192794 +Time = 0.0006625 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 11046 + Current mass in system = 1.05192e-09 + Linear momentum = (2.91612e-11 -9.57693e-09 0) + |Linear momentum| = 9.57698e-09 + Linear kinetic energy = 4.61857e-08 + model1: + number of parcels added = 11054 + mass introduced = 1.07235e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.138, 524.826 + Mass transfer phase change = 2.04307e-11 + D10, D32, Dmax (mu) = 48.2704, 80.1675, 149.517 + Liquid penetration 95% mass (m) = 0.00523299 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00371758, Final residual = 6.47098e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0160413, Final residual = 4.07898e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00237168, Final residual = 1.6503e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00265735, Final residual = 1.32753e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00288429, Final residual = 1.63451e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00288431, Final residual = 1.63584e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00202339, Final residual = 1.2896e-07, No Iterations 1 +min/max(T) = 618.962, 878.939 +GAMG: Solving for p, Initial residual = 0.0246352, Final residual = 0.000314291, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.15952e-06, global = 2.10379e-06, cumulative = 0.000470175 +GAMG: Solving for p, Initial residual = 0.000308202, Final residual = 5.31404e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.11445e-06, global = 2.11437e-06, cumulative = 0.000472289 +smoothSolver: Solving for epsilon, Initial residual = 0.0011449, Final residual = 2.01913e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00337937, Final residual = 5.67365e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097862 s +other Time = 0 s +rho Equations = 0.000168 s +U Equations = 0.00115 s +Y Equations = 0.00213022 s +E Equations = 0.0005 s +p Equations = 0.001849 s +calculate parcels = 21.423 s +chemistry correctThermo = 0.002013 s +turbulence correct = 0.000851 s +combustion correct(in Y) = 0.0890048 s +percentage of chemistry = 90.9493 % +percentage of rho/U/Y/E = 4.03448 % +========Time details of each equation======= +rhoEqn Time = 0.000287 s +rhoEqn assamble = 0.000228 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001148 s +UEqn assamble = 0.00067 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000478 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001471 s +YEqn assamble = 0.000552 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000379 s +EEqn assamble = 0.000284 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 44.67 s ClockTime = 45 s +Courant Number mean: 0.000321104 max: 0.0192386 +Time = 0.000665 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 11096 + Current mass in system = 1.05544e-09 + Linear momentum = (2.92139e-11 -9.5972e-09 0) + |Linear momentum| = 9.59724e-09 + Linear kinetic energy = 4.62229e-08 + model1: + number of parcels added = 11104 + mass introduced = 1.07605e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.149, 523.825 + Mass transfer phase change = 2.06147e-11 + D10, D32, Dmax (mu) = 48.2939, 80.2229, 149.522 + Liquid penetration 95% mass (m) = 0.00525023 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00387473, Final residual = 6.80635e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0164337, Final residual = 4.13028e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00235295, Final residual = 1.63555e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00264857, Final residual = 1.31948e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00287862, Final residual = 1.63595e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00287863, Final residual = 1.63728e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00201253, Final residual = 1.27272e-07, No Iterations 1 +min/max(T) = 618.928, 879.854 +GAMG: Solving for p, Initial residual = 0.02396, Final residual = 0.000248069, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.16186e-06, global = 2.11536e-06, cumulative = 0.000474405 +GAMG: Solving for p, Initial residual = 0.000242422, Final residual = 3.74847e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.12082e-06, global = 2.12075e-06, cumulative = 0.000476526 +smoothSolver: Solving for epsilon, Initial residual = 0.00114272, Final residual = 2.01501e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00335655, Final residual = 5.6342e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.066809 s +other Time = 0 s +rho Equations = 0.00017 s +U Equations = 0.001059 s +Y Equations = 0.00206406 s +E Equations = 0.000496 s +p Equations = 0.001858 s +calculate parcels = 21.5598 s +chemistry correctThermo = 0.001923 s +turbulence correct = 0.000813 s +combustion correct(in Y) = 0.0582489 s +percentage of chemistry = 87.1873 % +percentage of rho/U/Y/E = 5.67148 % +========Time details of each equation======= +rhoEqn Time = 0.00029 s +rhoEqn assamble = 0.000232 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001059 s +UEqn assamble = 0.000688 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000371 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001454 s +YEqn assamble = 0.000531 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000105 s +YEqn correct boundary = 0 s +EEqn Time = 0.000373 s +EEqn assamble = 0.000281 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 44.88 s ClockTime = 45 s +Courant Number mean: 0.000326309 max: 0.0191956 +Time = 0.0006675 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 57 new parcels + +Cloud: sprayCloud + Current number of parcels = 11153 + Current mass in system = 1.05948e-09 + Linear momentum = (2.96642e-11 -9.62291e-09 0) + |Linear momentum| = 9.62296e-09 + Linear kinetic energy = 4.62902e-08 + model1: + number of parcels added = 11161 + mass introduced = 1.08027e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.147, 522.76 + Mass transfer phase change = 2.07994e-11 + D10, D32, Dmax (mu) = 48.228, 80.2475, 149.527 + Liquid penetration 95% mass (m) = 0.00526624 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00391995, Final residual = 6.80114e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0168123, Final residual = 4.19689e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00233047, Final residual = 1.61202e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00264129, Final residual = 1.30931e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00287343, Final residual = 1.63639e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00287344, Final residual = 1.63772e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00200603, Final residual = 1.26148e-07, No Iterations 1 +min/max(T) = 618.911, 880.777 +GAMG: Solving for p, Initial residual = 0.024146, Final residual = 0.000232743, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.16534e-06, global = 2.12302e-06, cumulative = 0.000478649 +GAMG: Solving for p, Initial residual = 0.00022461, Final residual = 2.86317e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.12867e-06, global = 2.12862e-06, cumulative = 0.000480777 +smoothSolver: Solving for epsilon, Initial residual = 0.00114001, Final residual = 2.00989e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00333469, Final residual = 5.59493e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.124473 s +other Time = 0 s +rho Equations = 0.000206 s +U Equations = 0.00123 s +Y Equations = 0.00241619 s +E Equations = 0.000648 s +p Equations = 0.002345 s +calculate parcels = 21.7033 s +chemistry correctThermo = 0.002711 s +turbulence correct = 0.001 s +combustion correct(in Y) = 0.113709 s +percentage of chemistry = 91.3522 % +percentage of rho/U/Y/E = 3.61539 % +========Time details of each equation======= +rhoEqn Time = 0.000358 s +rhoEqn assamble = 0.000281 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00123 s +UEqn assamble = 0.000735 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000495 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001697 s +YEqn assamble = 0.000642 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000135 s +YEqn correct boundary = 0 s +EEqn Time = 0.000494 s +EEqn assamble = 0.000375 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000119 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 45.15 s ClockTime = 46 s +Courant Number mean: 0.000332534 max: 0.0191396 +Time = 0.00067 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 11201 + Current mass in system = 1.06285e-09 + Linear momentum = (3.03753e-11 -9.64151e-09 0) + |Linear momentum| = 9.64156e-09 + Linear kinetic energy = 4.63189e-08 + model1: + number of parcels added = 11209 + mass introduced = 1.08384e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.135, 521.645 + Mass transfer phase change = 2.09845e-11 + D10, D32, Dmax (mu) = 48.2317, 80.2952, 149.532 + Liquid penetration 95% mass (m) = 0.0052819 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00378309, Final residual = 6.62628e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0171726, Final residual = 4.27264e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00231537, Final residual = 1.5996e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00263276, Final residual = 1.29037e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00286774, Final residual = 1.63716e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00286775, Final residual = 1.63848e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00199951, Final residual = 1.23383e-07, No Iterations 1 +min/max(T) = 618.919, 881.709 +GAMG: Solving for p, Initial residual = 0.0242274, Final residual = 0.000244709, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.17376e-06, global = 2.13044e-06, cumulative = 0.000482908 +GAMG: Solving for p, Initial residual = 0.00023774, Final residual = 3.17911e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.13447e-06, global = 2.13441e-06, cumulative = 0.000485042 +smoothSolver: Solving for epsilon, Initial residual = 0.00113759, Final residual = 2.00503e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00331263, Final residual = 5.55599e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094041 s +other Time = 1e-06 s +rho Equations = 0.000169 s +U Equations = 0.001095 s +Y Equations = 0.00264733 s +E Equations = 0.0006 s +p Equations = 0.002176 s +calculate parcels = 21.894 s +chemistry correctThermo = 0.002778 s +turbulence correct = 0.000983 s +combustion correct(in Y) = 0.0833977 s +percentage of chemistry = 88.6822 % +percentage of rho/U/Y/E = 4.7972 % +========Time details of each equation======= +rhoEqn Time = 0.00031 s +rhoEqn assamble = 0.000245 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001094 s +UEqn assamble = 0.000664 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00043 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001404 s +YEqn assamble = 0.00064 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -0.000128 s +YEqn correct boundary = 0 s +EEqn Time = 0.000445 s +EEqn assamble = 0.000331 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 45.43 s ClockTime = 46 s +Courant Number mean: 0.000338872 max: 0.0190935 +Time = 0.0006725 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 11252 + Current mass in system = 1.06644e-09 + Linear momentum = (3.0338e-11 -9.66223e-09 0) + |Linear momentum| = 9.66228e-09 + Linear kinetic energy = 4.63591e-08 + model1: + number of parcels added = 11260 + mass introduced = 1.08761e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.139, 520.503 + Mass transfer phase change = 2.11705e-11 + D10, D32, Dmax (mu) = 48.2452, 80.3336, 149.537 + Liquid penetration 95% mass (m) = 0.00529728 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00366389, Final residual = 6.33085e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0174256, Final residual = 4.33085e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00231998, Final residual = 1.57879e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00262632, Final residual = 1.2844e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00286312, Final residual = 1.63712e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00286313, Final residual = 1.63843e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00199364, Final residual = 1.2045e-07, No Iterations 1 +min/max(T) = 618.926, 882.651 +GAMG: Solving for p, Initial residual = 0.0247373, Final residual = 0.000253412, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.18005e-06, global = 2.13643e-06, cumulative = 0.000487179 +GAMG: Solving for p, Initial residual = 0.000246323, Final residual = 2.0415e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.14295e-06, global = 2.14291e-06, cumulative = 0.000489321 +smoothSolver: Solving for epsilon, Initial residual = 0.001135, Final residual = 1.99952e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00329069, Final residual = 5.51607e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.091715 s +other Time = 0 s +rho Equations = 0.00015 s +U Equations = 0.000951 s +Y Equations = 0.0023151 s +E Equations = 0.000626 s +p Equations = 0.002231 s +calculate parcels = 22.0746 s +chemistry correctThermo = 0.002863 s +turbulence correct = 0.000972 s +combustion correct(in Y) = 0.0814019 s +percentage of chemistry = 88.7553 % +percentage of rho/U/Y/E = 4.40724 % +========Time details of each equation======= +rhoEqn Time = 0.000296 s +rhoEqn assamble = 0.000233 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000951 s +UEqn assamble = 0.00058 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000371 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001755 s +YEqn assamble = 0.00063 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000232 s +YEqn correct boundary = 0 s +EEqn Time = 0.000456 s +EEqn assamble = 0.00034 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 45.7 s ClockTime = 46 s +Courant Number mean: 0.000345281 max: 0.0190831 +Time = 0.000675 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 54 new parcels + +Cloud: sprayCloud + Current number of parcels = 11306 + Current mass in system = 1.07023e-09 + Linear momentum = (2.91214e-11 -9.68512e-09 0) + |Linear momentum| = 9.68517e-09 + Linear kinetic energy = 4.64109e-08 + model1: + number of parcels added = 11314 + mass introduced = 1.09159e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.141, 519.396 + Mass transfer phase change = 2.13572e-11 + D10, D32, Dmax (mu) = 48.2633, 80.3823, 149.542 + Liquid penetration 95% mass (m) = 0.00531404 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00356894, Final residual = 6.09229e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.01764, Final residual = 4.37589e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00230608, Final residual = 1.56084e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00261967, Final residual = 1.27615e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00285798, Final residual = 1.63687e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00285799, Final residual = 1.63819e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0019896, Final residual = 1.18106e-07, No Iterations 1 +min/max(T) = 618.952, 883.601 +GAMG: Solving for p, Initial residual = 0.0245172, Final residual = 0.000166121, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.17918e-06, global = 2.14789e-06, cumulative = 0.000491469 +GAMG: Solving for p, Initial residual = 0.000160111, Final residual = 1.92635e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.15182e-06, global = 2.15179e-06, cumulative = 0.000493621 +smoothSolver: Solving for epsilon, Initial residual = 0.00113195, Final residual = 1.99326e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00326865, Final residual = 5.47548e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.0813 s +other Time = 0 s +rho Equations = 0.000172 s +U Equations = 0.001167 s +Y Equations = 0.00259518 s +E Equations = 0.000653 s +p Equations = 0.002242 s +calculate parcels = 22.2693 s +chemistry correctThermo = 0.002955 s +turbulence correct = 0.001043 s +combustion correct(in Y) = 0.0702678 s +percentage of chemistry = 86.4303 % +percentage of rho/U/Y/E = 5.64229 % +========Time details of each equation======= +rhoEqn Time = 0.000314 s +rhoEqn assamble = 0.000247 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001165 s +UEqn assamble = 0.000677 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000488 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00195 s +YEqn assamble = 0.000712 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000222 s +YEqn correct boundary = 0 s +EEqn Time = 0.000483 s +EEqn assamble = 0.000352 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000131 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 45.97 s ClockTime = 46 s +Courant Number mean: 0.000351781 max: 0.0190592 +Time = 0.0006775 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 41 new parcels + +Cloud: sprayCloud + Current number of parcels = 11347 + Current mass in system = 1.07307e-09 + Linear momentum = (2.90091e-11 -9.69785e-09 0) + |Linear momentum| = 9.69789e-09 + Linear kinetic energy = 4.64074e-08 + model1: + number of parcels added = 11355 + mass introduced = 1.09461e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.152, 518.398 + Mass transfer phase change = 2.15446e-11 + D10, D32, Dmax (mu) = 48.2523, 80.4111, 149.548 + Liquid penetration 95% mass (m) = 0.00533023 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00354495, Final residual = 6.06872e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0177729, Final residual = 4.39495e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00228822, Final residual = 1.54548e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00261349, Final residual = 1.27229e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00285339, Final residual = 1.63665e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0028534, Final residual = 1.63796e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00198451, Final residual = 1.16679e-07, No Iterations 1 +min/max(T) = 618.992, 884.559 +GAMG: Solving for p, Initial residual = 0.0246174, Final residual = 0.000164914, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.19037e-06, global = 2.15673e-06, cumulative = 0.000495778 +GAMG: Solving for p, Initial residual = 0.000157146, Final residual = 1.978e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.16082e-06, global = 2.16079e-06, cumulative = 0.000497939 +smoothSolver: Solving for epsilon, Initial residual = 0.00112919, Final residual = 1.98662e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00324646, Final residual = 5.43465e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097988 s +other Time = 0 s +rho Equations = 0.000139 s +U Equations = 0.00092 s +Y Equations = 0.0023491 s +E Equations = 0.000602 s +p Equations = 0.002196 s +calculate parcels = 22.4672 s +chemistry correctThermo = 0.002807 s +turbulence correct = 0.001001 s +combustion correct(in Y) = 0.0877939 s +percentage of chemistry = 89.5966 % +percentage of rho/U/Y/E = 4.09244 % +========Time details of each equation======= +rhoEqn Time = 0.000282 s +rhoEqn assamble = 0.000224 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000919 s +UEqn assamble = 0.000557 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000362 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001808 s +YEqn assamble = 0.000661 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000216 s +YEqn correct boundary = 0 s +EEqn Time = 0.000442 s +EEqn assamble = 0.000329 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 46.28 s ClockTime = 47 s +Courant Number mean: 0.000358377 max: 0.0190182 +Time = 0.00068 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 11397 + Current mass in system = 1.07654e-09 + Linear momentum = (2.88672e-11 -9.71725e-09 0) + |Linear momentum| = 9.71729e-09 + Linear kinetic energy = 4.64398e-08 + model1: + number of parcels added = 11405 + mass introduced = 1.09827e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.14, 517.532 + Mass transfer phase change = 2.17329e-11 + D10, D32, Dmax (mu) = 48.2565, 80.4531, 149.553 + Liquid penetration 95% mass (m) = 0.00534776 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00360192, Final residual = 6.23531e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0178448, Final residual = 4.40232e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00227277, Final residual = 1.53107e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00260776, Final residual = 1.26706e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00284897, Final residual = 1.63564e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00284898, Final residual = 1.63695e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00198112, Final residual = 1.1479e-07, No Iterations 1 +min/max(T) = 619.054, 885.527 +GAMG: Solving for p, Initial residual = 0.0246706, Final residual = 0.00014128, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.19679e-06, global = 2.16578e-06, cumulative = 0.000500104 +GAMG: Solving for p, Initial residual = 0.000136164, Final residual = 1.6245e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.17037e-06, global = 2.17034e-06, cumulative = 0.000502275 +smoothSolver: Solving for epsilon, Initial residual = 0.00112894, Final residual = 1.97959e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00322416, Final residual = 5.39363e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092936 s +other Time = 0 s +rho Equations = 0.000163 s +U Equations = 0.001119 s +Y Equations = 0.00223192 s +E Equations = 0.000588 s +p Equations = 0.002093 s +calculate parcels = 22.6532 s +chemistry correctThermo = 0.002779 s +turbulence correct = 0.000916 s +combustion correct(in Y) = 0.0828451 s +percentage of chemistry = 89.1421 % +percentage of rho/U/Y/E = 4.41371 % +========Time details of each equation======= +rhoEqn Time = 0.000298 s +rhoEqn assamble = 0.000232 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001119 s +UEqn assamble = 0.000682 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000437 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001554 s +YEqn assamble = 0.000596 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000139 s +YEqn correct boundary = 0 s +EEqn Time = 0.000438 s +EEqn assamble = 0.000324 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 46.56 s ClockTime = 47 s +Courant Number mean: 0.000365094 max: 0.0189816 +Time = 0.0006825 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 11445 + Current mass in system = 1.07986e-09 + Linear momentum = (2.83895e-11 -9.73487e-09 0) + |Linear momentum| = 9.73491e-09 + Linear kinetic energy = 4.64623e-08 + model1: + number of parcels added = 11453 + mass introduced = 1.10178e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.142, 516.8 + Mass transfer phase change = 2.19222e-11 + D10, D32, Dmax (mu) = 48.0925, 80.444, 149.558 + Liquid penetration 95% mass (m) = 0.00536463 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00367903, Final residual = 6.37681e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0178961, Final residual = 4.40092e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00226128, Final residual = 1.51671e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00260257, Final residual = 1.26059e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00284422, Final residual = 1.63471e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00284424, Final residual = 1.63601e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00198277, Final residual = 1.12813e-07, No Iterations 1 +min/max(T) = 619.141, 886.504 +GAMG: Solving for p, Initial residual = 0.0250183, Final residual = 0.000203864, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.21665e-06, global = 2.1735e-06, cumulative = 0.000504448 +GAMG: Solving for p, Initial residual = 0.000197423, Final residual = 3.19341e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.1812e-06, global = 2.18114e-06, cumulative = 0.000506629 +smoothSolver: Solving for epsilon, Initial residual = 0.00112881, Final residual = 1.97135e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00320244, Final residual = 5.3521e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.089898 s +other Time = 0 s +rho Equations = 0.000173 s +U Equations = 0.00121 s +Y Equations = 0.00205208 s +E Equations = 0.000523 s +p Equations = 0.001787 s +calculate parcels = 22.853 s +chemistry correctThermo = 0.001954 s +turbulence correct = 0.000832 s +combustion correct(in Y) = 0.0811809 s +percentage of chemistry = 90.3034 % +percentage of rho/U/Y/E = 4.40285 % +========Time details of each equation======= +rhoEqn Time = 0.000287 s +rhoEqn assamble = 0.000226 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001209 s +UEqn assamble = 0.000727 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000482 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001407 s +YEqn assamble = 0.000526 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000114 s +YEqn correct boundary = 0 s +EEqn Time = 0.000385 s +EEqn assamble = 0.000285 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.0001 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 46.85 s ClockTime = 47 s +Courant Number mean: 0.000371954 max: 0.018944 +Time = 0.000685 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 45 new parcels + +Cloud: sprayCloud + Current number of parcels = 11490 + Current mass in system = 1.08294e-09 + Linear momentum = (2.84303e-11 -9.74994e-09 0) + |Linear momentum| = 9.74998e-09 + Linear kinetic energy = 4.64712e-08 + model1: + number of parcels added = 11498 + mass introduced = 1.10506e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.143, 516.186 + Mass transfer phase change = 2.21122e-11 + D10, D32, Dmax (mu) = 47.5902, 80.4201, 149.563 + Liquid penetration 95% mass (m) = 0.00538262 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00361482, Final residual = 6.20228e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0179294, Final residual = 4.40209e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00225113, Final residual = 1.47322e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00259707, Final residual = 1.25742e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00283977, Final residual = 1.63396e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00283978, Final residual = 1.63528e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00198435, Final residual = 1.1063e-07, No Iterations 1 +min/max(T) = 619.224, 887.488 +GAMG: Solving for p, Initial residual = 0.0248342, Final residual = 0.000189172, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.22483e-06, global = 2.183e-06, cumulative = 0.000508812 +GAMG: Solving for p, Initial residual = 0.000181709, Final residual = 2.71096e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.1906e-06, global = 2.19055e-06, cumulative = 0.000511003 +smoothSolver: Solving for epsilon, Initial residual = 0.00112846, Final residual = 1.96257e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00318093, Final residual = 5.31043e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.074494 s +other Time = 0 s +rho Equations = 0.000184 s +U Equations = 0.00114 s +Y Equations = 0.00221092 s +E Equations = 0.000503 s +p Equations = 0.001863 s +calculate parcels = 23.0733 s +chemistry correctThermo = 0.00191 s +turbulence correct = 0.0009 s +combustion correct(in Y) = 0.0655221 s +percentage of chemistry = 87.9562 % +percentage of rho/U/Y/E = 5.42047 % +========Time details of each equation======= +rhoEqn Time = 0.000302 s +rhoEqn assamble = 0.000238 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001139 s +UEqn assamble = 0.000698 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000441 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001542 s +YEqn assamble = 0.000564 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.6e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000377 s +EEqn assamble = 0.000284 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 47.14 s ClockTime = 48 s +Courant Number mean: 0.000378878 max: 0.0188874 +Time = 0.0006875 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 11540 + Current mass in system = 1.08638e-09 + Linear momentum = (2.92885e-11 -9.76858e-09 0) + |Linear momentum| = 9.76863e-09 + Linear kinetic energy = 4.6499e-08 + model1: + number of parcels added = 11548 + mass introduced = 1.10868e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.139, 515.673 + Mass transfer phase change = 2.2303e-11 + D10, D32, Dmax (mu) = 47.6095, 80.4776, 149.569 + Liquid penetration 95% mass (m) = 0.00539999 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00358491, Final residual = 5.93839e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0179482, Final residual = 4.4056e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.002245, Final residual = 1.45338e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00259106, Final residual = 1.25394e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00283491, Final residual = 1.63247e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00283492, Final residual = 1.63379e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00198158, Final residual = 1.08596e-07, No Iterations 1 +min/max(T) = 619.32, 888.482 +GAMG: Solving for p, Initial residual = 0.0244646, Final residual = 0.000182024, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.2337e-06, global = 2.19133e-06, cumulative = 0.000513194 +GAMG: Solving for p, Initial residual = 0.000174922, Final residual = 2.95229e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.19881e-06, global = 2.19874e-06, cumulative = 0.000515393 +smoothSolver: Solving for epsilon, Initial residual = 0.00112774, Final residual = 1.95526e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0031592, Final residual = 5.26923e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.069986 s +other Time = 0 s +rho Equations = 0.000151 s +U Equations = 0.00096 s +Y Equations = 0.00259447 s +E Equations = 0.000515 s +p Equations = 0.001902 s +calculate parcels = 23.2155 s +chemistry correctThermo = 0.001879 s +turbulence correct = 0.000921 s +combustion correct(in Y) = 0.0608835 s +percentage of chemistry = 86.9939 % +percentage of rho/U/Y/E = 6.03045 % +========Time details of each equation======= +rhoEqn Time = 0.000276 s +rhoEqn assamble = 0.000221 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000958 s +UEqn assamble = 0.000602 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000356 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002032 s +YEqn assamble = 0.000743 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000252 s +YEqn correct boundary = 0 s +EEqn Time = 0.000388 s +EEqn assamble = 0.000296 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 47.35 s ClockTime = 48 s +Courant Number mean: 0.000385825 max: 0.0188493 +Time = 0.00069 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 11590 + Current mass in system = 1.0898e-09 + Linear momentum = (2.89033e-11 -9.78713e-09 0) + |Linear momentum| = 9.78718e-09 + Linear kinetic energy = 4.65259e-08 + model1: + number of parcels added = 11598 + mass introduced = 1.11229e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.131, 515.255 + Mass transfer phase change = 2.24946e-11 + D10, D32, Dmax (mu) = 47.6296, 80.5309, 149.574 + Liquid penetration 95% mass (m) = 0.0054165 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00343001, Final residual = 5.68794e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.017858, Final residual = 4.3628e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00222279, Final residual = 1.44998e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00258586, Final residual = 1.2463e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00283064, Final residual = 1.6316e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00283065, Final residual = 1.6329e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00197912, Final residual = 1.0628e-07, No Iterations 1 +min/max(T) = 619.422, 889.485 +GAMG: Solving for p, Initial residual = 0.0246566, Final residual = 0.000190644, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.24354e-06, global = 2.20086e-06, cumulative = 0.000517594 +GAMG: Solving for p, Initial residual = 0.000183765, Final residual = 2.12592e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.20805e-06, global = 2.208e-06, cumulative = 0.000519802 +smoothSolver: Solving for epsilon, Initial residual = 0.00112638, Final residual = 1.94767e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00313705, Final residual = 5.22799e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.091814 s +other Time = 1e-06 s +rho Equations = 0.000191 s +U Equations = 0.001151 s +Y Equations = 0.00240541 s +E Equations = 0.000621 s +p Equations = 0.002008 s +calculate parcels = 23.3642 s +chemistry correctThermo = 0.002892 s +turbulence correct = 0.000941 s +combustion correct(in Y) = 0.0813936 s +percentage of chemistry = 88.6505 % +percentage of rho/U/Y/E = 4.75789 % +========Time details of each equation======= +rhoEqn Time = 0.000314 s +rhoEqn assamble = 0.00025 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001149 s +UEqn assamble = 0.000712 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000437 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001742 s +YEqn assamble = 0.000657 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00017 s +YEqn correct boundary = 0 s +EEqn Time = 0.000462 s +EEqn assamble = 0.000345 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 47.59 s ClockTime = 48 s +Courant Number mean: 0.000392774 max: 0.0187961 +Time = 0.0006925 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 11637 + Current mass in system = 1.09306e-09 + Linear momentum = (2.95363e-11 -9.80402e-09 0) + |Linear momentum| = 9.80407e-09 + Linear kinetic energy = 4.65438e-08 + model1: + number of parcels added = 11646 + mass introduced = 1.11575e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.138, 514.927 + Mass transfer phase change = 2.26877e-11 + D10, D32, Dmax (mu) = 49.56, 80.5803, 149.579 + Liquid penetration 95% mass (m) = 0.00543246 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00337849, Final residual = 5.64917e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0177687, Final residual = 4.33001e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00222159, Final residual = 1.46452e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00258427, Final residual = 1.25322e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00282589, Final residual = 1.62964e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0028259, Final residual = 1.63094e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00197829, Final residual = 1.04833e-07, No Iterations 1 +min/max(T) = 619.535, 890.499 +GAMG: Solving for p, Initial residual = 0.0246574, Final residual = 0.000180373, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.26148e-06, global = 2.21923e-06, cumulative = 0.000522021 +GAMG: Solving for p, Initial residual = 0.000172829, Final residual = 1.79307e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.22676e-06, global = 2.22672e-06, cumulative = 0.000524248 +smoothSolver: Solving for epsilon, Initial residual = 0.00112522, Final residual = 1.94001e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00311518, Final residual = 5.18802e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.090785 s +other Time = 1e-06 s +rho Equations = 0.000144 s +U Equations = 0.000956 s +Y Equations = 0.00236577 s +E Equations = 0.000612 s +p Equations = 0.00189 s +calculate parcels = 23.5699 s +chemistry correctThermo = 0.002433 s +turbulence correct = 0.000821 s +combustion correct(in Y) = 0.0813902 s +percentage of chemistry = 89.6516 % +percentage of rho/U/Y/E = 4.49167 % +========Time details of each equation======= +rhoEqn Time = 0.000271 s +rhoEqn assamble = 0.000213 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000955 s +UEqn assamble = 0.000589 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000366 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001816 s +YEqn assamble = 0.000645 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000232 s +YEqn correct boundary = 0 s +EEqn Time = 0.000459 s +EEqn assamble = 0.000346 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 47.89 s ClockTime = 48 s +Courant Number mean: 0.000399747 max: 0.018773 +Time = 0.000695 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 38 new parcels + +Cloud: sprayCloud + Current number of parcels = 11675 + Current mass in system = 1.0956e-09 + Linear momentum = (2.8854e-11 -9.81323e-09 0) + |Linear momentum| = 9.81328e-09 + Linear kinetic energy = 4.65213e-08 + model1: + number of parcels added = 11684 + mass introduced = 1.11848e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.135, 514.668 + Mass transfer phase change = 2.28804e-11 + D10, D32, Dmax (mu) = 49.5691, 80.6025, 149.585 + Liquid penetration 95% mass (m) = 0.00544841 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00326722, Final residual = 5.54939e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0176492, Final residual = 4.30484e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00222241, Final residual = 1.45694e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00257283, Final residual = 1.22672e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00282189, Final residual = 1.62953e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0028219, Final residual = 1.63083e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00197454, Final residual = 1.01601e-07, No Iterations 1 +min/max(T) = 619.259, 891.521 +GAMG: Solving for p, Initial residual = 0.0246597, Final residual = 0.00018991, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.26018e-06, global = 2.21296e-06, cumulative = 0.000526461 +GAMG: Solving for p, Initial residual = 0.000181866, Final residual = 2.48519e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.22086e-06, global = 2.2208e-06, cumulative = 0.000528682 +smoothSolver: Solving for epsilon, Initial residual = 0.00112395, Final residual = 1.93357e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00309394, Final residual = 5.14992e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.072358 s +other Time = 0 s +rho Equations = 0.000143 s +U Equations = 0.000923 s +Y Equations = 0.00204522 s +E Equations = 0.000498 s +p Equations = 0.001891 s +calculate parcels = 23.7566 s +chemistry correctThermo = 0.002001 s +turbulence correct = 0.000827 s +combustion correct(in Y) = 0.0638688 s +percentage of chemistry = 88.2677 % +percentage of rho/U/Y/E = 4.98801 % +========Time details of each equation======= +rhoEqn Time = 0.000262 s +rhoEqn assamble = 0.000208 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000923 s +UEqn assamble = 0.000565 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000358 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001495 s +YEqn assamble = 0.000558 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000146 s +YEqn correct boundary = 0 s +EEqn Time = 0.000377 s +EEqn assamble = 0.00028 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.7e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 48.15 s ClockTime = 49 s +Courant Number mean: 0.0004066 max: 0.0186976 +Time = 0.0006975 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 55 new parcels + +Cloud: sprayCloud + Current number of parcels = 11730 + Current mass in system = 1.09933e-09 + Linear momentum = (2.86097e-11 -9.83477e-09 0) + |Linear momentum| = 9.83481e-09 + Linear kinetic energy = 4.65637e-08 + model1: + number of parcels added = 11739 + mass introduced = 1.1224e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.14, 514.465 + Mass transfer phase change = 2.3074e-11 + D10, D32, Dmax (mu) = 49.5817, 80.6462, 149.59 + Liquid penetration 95% mass (m) = 0.00546526 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00338057, Final residual = 5.58036e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.017505, Final residual = 4.31788e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00222257, Final residual = 1.45606e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00256863, Final residual = 1.22715e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00281836, Final residual = 1.62817e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00281837, Final residual = 1.62946e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196973, Final residual = 1.006e-07, No Iterations 1 +min/max(T) = 619.002, 892.553 +GAMG: Solving for p, Initial residual = 0.0248657, Final residual = 0.000185895, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.26932e-06, global = 2.22272e-06, cumulative = 0.000530904 +GAMG: Solving for p, Initial residual = 0.00017963, Final residual = 1.838e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.23089e-06, global = 2.23085e-06, cumulative = 0.000533135 +smoothSolver: Solving for epsilon, Initial residual = 0.00112265, Final residual = 1.92571e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00307284, Final residual = 5.11114e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.089441 s +other Time = 0 s +rho Equations = 0.000137 s +U Equations = 0.000913 s +Y Equations = 0.00202523 s +E Equations = 0.000497 s +p Equations = 0.002383 s +calculate parcels = 23.9534 s +chemistry correctThermo = 0.002148 s +turbulence correct = 0.000992 s +combustion correct(in Y) = 0.0801678 s +percentage of chemistry = 89.632 % +percentage of rho/U/Y/E = 3.99395 % +========Time details of each equation======= +rhoEqn Time = 0.000288 s +rhoEqn assamble = 0.000227 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000912 s +UEqn assamble = 0.000552 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00036 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001468 s +YEqn assamble = 0.000549 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000136 s +YEqn correct boundary = 0 s +EEqn Time = 0.000374 s +EEqn assamble = 0.00028 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 48.44 s ClockTime = 49 s +Courant Number mean: 0.000413479 max: 0.0186689 +Time = 0.0007 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 47 new parcels + +Cloud: sprayCloud + Current number of parcels = 11777 + Current mass in system = 1.10248e-09 + Linear momentum = (2.80469e-11 -9.85031e-09 0) + |Linear momentum| = 9.85035e-09 + Linear kinetic energy = 4.65745e-08 + model1: + number of parcels added = 11786 + mass introduced = 1.12575e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.137, 514.296 + Mass transfer phase change = 2.32683e-11 + D10, D32, Dmax (mu) = 49.6018, 80.6858, 149.785 + Liquid penetration 95% mass (m) = 0.00548222 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00328188, Final residual = 5.28964e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0173451, Final residual = 4.28506e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00222435, Final residual = 1.46026e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00256316, Final residual = 1.22637e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00281387, Final residual = 1.62687e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00281388, Final residual = 1.62816e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196642, Final residual = 9.95972e-08, No Iterations 1 +min/max(T) = 618.744, 893.594 +GAMG: Solving for p, Initial residual = 0.0245422, Final residual = 0.000169789, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.27622e-06, global = 2.23179e-06, cumulative = 0.000535367 +GAMG: Solving for p, Initial residual = 0.000163913, Final residual = 1.30369e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.23946e-06, global = 2.23943e-06, cumulative = 0.000537606 +smoothSolver: Solving for epsilon, Initial residual = 0.00112059, Final residual = 1.9174e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00305102, Final residual = 5.07106e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.089557 s +other Time = 0 s +rho Equations = 0.00016 s +U Equations = 0.001086 s +Y Equations = 0.00233584 s +E Equations = 0.000612 s +p Equations = 0.001958 s +calculate parcels = 24.1522 s +chemistry correctThermo = 0.002788 s +turbulence correct = 0.000923 s +combustion correct(in Y) = 0.0795092 s +percentage of chemistry = 88.7805 % +percentage of rho/U/Y/E = 4.68287 % +========Time details of each equation======= +rhoEqn Time = 0.000289 s +rhoEqn assamble = 0.000218 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001084 s +UEqn assamble = 0.000659 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000425 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001693 s +YEqn assamble = 0.000635 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000172 s +YEqn correct boundary = 0 s +EEqn Time = 0.00046 s +EEqn assamble = 0.000344 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 48.91 s ClockTime = 49 s +Courant Number mean: 0.000420385 max: 0.0186673 +Time = 0.0007025 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 54 new parcels + +Cloud: sprayCloud + Current number of parcels = 11831 + Current mass in system = 1.10611e-09 + Linear momentum = (2.76328e-11 -9.87081e-09 0) + |Linear momentum| = 9.87085e-09 + Linear kinetic energy = 4.66112e-08 + model1: + number of parcels added = 11840 + mass introduced = 1.12958e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.142, 514.151 + Mass transfer phase change = 2.34634e-11 + D10, D32, Dmax (mu) = 49.6066, 80.7261, 149.708 + Liquid penetration 95% mass (m) = 0.00549883 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00349095, Final residual = 5.55303e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0171762, Final residual = 4.23159e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00221625, Final residual = 1.44453e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00255908, Final residual = 1.22506e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00281067, Final residual = 1.62545e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00281068, Final residual = 1.62674e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196537, Final residual = 9.93053e-08, No Iterations 1 +min/max(T) = 618.484, 894.642 +GAMG: Solving for p, Initial residual = 0.0244848, Final residual = 0.000172963, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.28989e-06, global = 2.24148e-06, cumulative = 0.000539848 +GAMG: Solving for p, Initial residual = 0.000167534, Final residual = 1.84895e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.24928e-06, global = 2.24923e-06, cumulative = 0.000542097 +smoothSolver: Solving for epsilon, Initial residual = 0.00111821, Final residual = 1.90866e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00302943, Final residual = 5.03078e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.077417 s +other Time = 0 s +rho Equations = 0.000138 s +U Equations = 0.000986 s +Y Equations = 0.00206856 s +E Equations = 0.00049 s +p Equations = 0.001856 s +calculate parcels = 24.3311 s +chemistry correctThermo = 0.001961 s +turbulence correct = 0.00084 s +combustion correct(in Y) = 0.0688814 s +percentage of chemistry = 88.9746 % +percentage of rho/U/Y/E = 4.75678 % +========Time details of each equation======= +rhoEqn Time = 0.000286 s +rhoEqn assamble = 0.00023 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000985 s +UEqn assamble = 0.000618 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000367 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001523 s +YEqn assamble = 0.000546 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000181 s +YEqn correct boundary = 0 s +EEqn Time = 0.00037 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 49.17 s ClockTime = 50 s +Courant Number mean: 0.000427352 max: 0.0186376 +Time = 0.000705 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 40 new parcels + +Cloud: sprayCloud + Current number of parcels = 11871 + Current mass in system = 1.10875e-09 + Linear momentum = (2.76633e-11 -9.88101e-09 0) + |Linear momentum| = 9.88104e-09 + Linear kinetic energy = 4.6594e-08 + model1: + number of parcels added = 11880 + mass introduced = 1.13241e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.153, 513.998 + Mass transfer phase change = 2.36593e-11 + D10, D32, Dmax (mu) = 49.6188, 80.7511, 149.609 + Liquid penetration 95% mass (m) = 0.00551538 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00356085, Final residual = 5.68421e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0169989, Final residual = 4.18703e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00222069, Final residual = 1.45736e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0025544, Final residual = 1.21524e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00280686, Final residual = 1.62332e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00280687, Final residual = 1.6246e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196397, Final residual = 9.82823e-08, No Iterations 1 +min/max(T) = 618.231, 895.7 +GAMG: Solving for p, Initial residual = 0.0245036, Final residual = 0.000165865, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.29762e-06, global = 2.25101e-06, cumulative = 0.000544348 +GAMG: Solving for p, Initial residual = 0.000160292, Final residual = 1.63967e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.2584e-06, global = 2.25836e-06, cumulative = 0.000546606 +smoothSolver: Solving for epsilon, Initial residual = 0.0011155, Final residual = 1.9e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00300763, Final residual = 4.98991e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.088895 s +other Time = 1e-06 s +rho Equations = 0.000163 s +U Equations = 0.001233 s +Y Equations = 0.0024209 s +E Equations = 0.000597 s +p Equations = 0.002219 s +calculate parcels = 24.5067 s +chemistry correctThermo = 0.002792 s +turbulence correct = 0.000996 s +combustion correct(in Y) = 0.0782791 s +percentage of chemistry = 88.0579 % +percentage of rho/U/Y/E = 4.9653 % +========Time details of each equation======= +rhoEqn Time = 0.00031 s +rhoEqn assamble = 0.000246 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001231 s +UEqn assamble = 0.000775 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000456 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001758 s +YEqn assamble = 0.000677 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000165 s +YEqn correct boundary = 0 s +EEqn Time = 0.000444 s +EEqn assamble = 0.000333 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 49.43 s ClockTime = 50 s +Courant Number mean: 0.000434333 max: 0.0185944 +Time = 0.0007075 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 47 new parcels + +Cloud: sprayCloud + Current number of parcels = 11918 + Current mass in system = 1.11186e-09 + Linear momentum = (2.72104e-11 -9.896e-09 0) + |Linear momentum| = 9.89604e-09 + Linear kinetic energy = 4.6602e-08 + model1: + number of parcels added = 11927 + mass introduced = 1.13572e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.13, 514.224 + Mass transfer phase change = 2.38561e-11 + D10, D32, Dmax (mu) = 49.624, 80.7933, 149.683 + Liquid penetration 95% mass (m) = 0.00553186 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00379617, Final residual = 5.94842e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0168056, Final residual = 4.14787e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00220941, Final residual = 1.42193e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00255006, Final residual = 1.2082e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00280321, Final residual = 1.62321e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00280322, Final residual = 1.62449e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196347, Final residual = 9.66258e-08, No Iterations 1 +min/max(T) = 617.979, 896.767 +GAMG: Solving for p, Initial residual = 0.0246342, Final residual = 0.000158423, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.30278e-06, global = 2.26098e-06, cumulative = 0.000548867 +GAMG: Solving for p, Initial residual = 0.000153071, Final residual = 8.58067e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.26808e-06, global = 2.26785e-06, cumulative = 0.000551135 +smoothSolver: Solving for epsilon, Initial residual = 0.00111314, Final residual = 1.8917e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00298637, Final residual = 4.95166e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.068665 s +other Time = 0 s +rho Equations = 0.000158 s +U Equations = 0.001068 s +Y Equations = 0.00240371 s +E Equations = 0.000507 s +p Equations = 0.001817 s +calculate parcels = 24.679 s +chemistry correctThermo = 0.002135 s +turbulence correct = 0.000908 s +combustion correct(in Y) = 0.0594843 s +percentage of chemistry = 86.6297 % +percentage of rho/U/Y/E = 6.02449 % +========Time details of each equation======= +rhoEqn Time = 0.000285 s +rhoEqn assamble = 0.000228 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001067 s +UEqn assamble = 0.000687 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00038 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001809 s +YEqn assamble = 0.000615 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000139 s +YEqn correct boundary = 0 s +EEqn Time = 0.000382 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 49.68 s ClockTime = 50 s +Courant Number mean: 0.000441394 max: 0.0185675 +Time = 0.00071 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 57 new parcels + +Cloud: sprayCloud + Current number of parcels = 11975 + Current mass in system = 1.11566e-09 + Linear momentum = (2.6949e-11 -9.91804e-09 0) + |Linear momentum| = 9.91808e-09 + Linear kinetic energy = 4.66464e-08 + model1: + number of parcels added = 11984 + mass introduced = 1.13972e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.137, 514.455 + Mass transfer phase change = 2.40537e-11 + D10, D32, Dmax (mu) = 49.6179, 80.8358, 149.629 + Liquid penetration 95% mass (m) = 0.00554938 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00395299, Final residual = 6.22309e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0166121, Final residual = 4.09819e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00220072, Final residual = 1.4047e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00254621, Final residual = 1.20278e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00279975, Final residual = 1.62232e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00279976, Final residual = 1.6236e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196609, Final residual = 9.70638e-08, No Iterations 1 +min/max(T) = 617.732, 897.844 +GAMG: Solving for p, Initial residual = 0.0245764, Final residual = 0.000149101, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.31314e-06, global = 2.27107e-06, cumulative = 0.000553406 +GAMG: Solving for p, Initial residual = 0.000143979, Final residual = 1.59752e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.27794e-06, global = 2.2779e-06, cumulative = 0.000555684 +smoothSolver: Solving for epsilon, Initial residual = 0.00111038, Final residual = 1.88354e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00296505, Final residual = 4.91295e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.0667 s +other Time = 0 s +rho Equations = 0.000156 s +U Equations = 0.000941 s +Y Equations = 0.00227752 s +E Equations = 0.000522 s +p Equations = 0.001967 s +calculate parcels = 24.8247 s +chemistry correctThermo = 0.00192 s +turbulence correct = 0.001351 s +combustion correct(in Y) = 0.0573885 s +percentage of chemistry = 86.0397 % +percentage of rho/U/Y/E = 5.84186 % +========Time details of each equation======= +rhoEqn Time = 0.000291 s +rhoEqn assamble = 0.00023 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00094 s +UEqn assamble = 0.000594 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000346 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001722 s +YEqn assamble = 0.000597 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000203 s +YEqn correct boundary = 0 s +EEqn Time = 0.000397 s +EEqn assamble = 0.000301 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 49.89 s ClockTime = 50 s +Courant Number mean: 0.000448585 max: 0.0185386 +Time = 0.0007125 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 42 new parcels + +Cloud: sprayCloud + Current number of parcels = 12017 + Current mass in system = 1.11841e-09 + Linear momentum = (2.73794e-11 -9.92934e-09 0) + |Linear momentum| = 9.92937e-09 + Linear kinetic energy = 4.66353e-08 + model1: + number of parcels added = 12026 + mass introduced = 1.14267e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.13, 514.675 + Mass transfer phase change = 2.42522e-11 + D10, D32, Dmax (mu) = 49.6342, 80.8958, 149.622 + Liquid penetration 95% mass (m) = 0.00556573 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00392837, Final residual = 6.33659e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0163886, Final residual = 4.02446e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00218868, Final residual = 1.37442e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00254244, Final residual = 1.20159e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00279678, Final residual = 1.6216e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0027968, Final residual = 1.62288e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196542, Final residual = 9.70924e-08, No Iterations 1 +min/max(T) = 617.496, 898.93 +GAMG: Solving for p, Initial residual = 0.0247996, Final residual = 0.000159295, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.32575e-06, global = 2.28022e-06, cumulative = 0.000557964 +GAMG: Solving for p, Initial residual = 0.000154715, Final residual = 1.44778e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.28733e-06, global = 2.28729e-06, cumulative = 0.000560252 +smoothSolver: Solving for epsilon, Initial residual = 0.00110696, Final residual = 1.87442e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00294378, Final residual = 4.87244e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.088482 s +other Time = 1e-06 s +rho Equations = 0.000139 s +U Equations = 0.000958 s +Y Equations = 0.00209056 s +E Equations = 0.000515 s +p Equations = 0.001858 s +calculate parcels = 25.0214 s +chemistry correctThermo = 0.001987 s +turbulence correct = 0.000881 s +combustion correct(in Y) = 0.0798884 s +percentage of chemistry = 90.2878 % +percentage of rho/U/Y/E = 4.18453 % +========Time details of each equation======= +rhoEqn Time = 0.000261 s +rhoEqn assamble = 0.000209 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000956 s +UEqn assamble = 0.000584 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000372 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001528 s +YEqn assamble = 0.000559 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000154 s +YEqn correct boundary = 0 s +EEqn Time = 0.000396 s +EEqn assamble = 0.0003 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 50.17 s ClockTime = 51 s +Courant Number mean: 0.000455812 max: 0.0185084 +Time = 0.000715 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 12067 + Current mass in system = 1.12171e-09 + Linear momentum = (2.83412e-11 -9.94615e-09 0) + |Linear momentum| = 9.94619e-09 + Linear kinetic energy = 4.66525e-08 + model1: + number of parcels added = 12076 + mass introduced = 1.14616e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.127, 514.889 + Mass transfer phase change = 2.44516e-11 + D10, D32, Dmax (mu) = 48.8404, 80.8834, 149.798 + Liquid penetration 95% mass (m) = 0.00558307 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00388276, Final residual = 6.15061e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0161442, Final residual = 3.9598e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0021897, Final residual = 1.36966e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00253885, Final residual = 1.20696e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00279279, Final residual = 1.62107e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0027928, Final residual = 1.62234e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00197183, Final residual = 9.83731e-08, No Iterations 1 +min/max(T) = 617.252, 900.024 +GAMG: Solving for p, Initial residual = 0.0248819, Final residual = 0.000175716, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.34006e-06, global = 2.29105e-06, cumulative = 0.000562543 +GAMG: Solving for p, Initial residual = 0.000170314, Final residual = 3.27885e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.29893e-06, global = 2.29885e-06, cumulative = 0.000564842 +smoothSolver: Solving for epsilon, Initial residual = 0.00110372, Final residual = 1.86436e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00292587, Final residual = 4.83141e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094482 s +other Time = 0 s +rho Equations = 0.000167 s +U Equations = 0.001142 s +Y Equations = 0.00244462 s +E Equations = 0.000635 s +p Equations = 0.002308 s +calculate parcels = 25.2276 s +chemistry correctThermo = 0.002789 s +turbulence correct = 0.000969 s +combustion correct(in Y) = 0.0838344 s +percentage of chemistry = 88.7305 % +percentage of rho/U/Y/E = 4.64493 % +========Time details of each equation======= +rhoEqn Time = 0.000319 s +rhoEqn assamble = 0.000254 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001141 s +UEqn assamble = 0.00067 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000471 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001802 s +YEqn assamble = 0.000663 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000215 s +YEqn correct boundary = 0 s +EEqn Time = 0.000481 s +EEqn assamble = 0.000363 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 50.47 s ClockTime = 51 s +Courant Number mean: 0.000463165 max: 0.0184808 +Time = 0.0007175 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 41 new parcels + +Cloud: sprayCloud + Current number of parcels = 12108 + Current mass in system = 1.12436e-09 + Linear momentum = (2.83922e-11 -9.95653e-09 0) + |Linear momentum| = 9.95657e-09 + Linear kinetic energy = 4.66366e-08 + model1: + number of parcels added = 12117 + mass introduced = 1.14902e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.135, 515.091 + Mass transfer phase change = 2.46518e-11 + D10, D32, Dmax (mu) = 48.8561, 80.9397, 149.784 + Liquid penetration 95% mass (m) = 0.0056005 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00359016, Final residual = 5.99319e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0158804, Final residual = 3.89769e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0021858, Final residual = 1.36243e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00253404, Final residual = 1.20609e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00278942, Final residual = 1.61989e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00278943, Final residual = 1.62119e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0019679, Final residual = 9.73444e-08, No Iterations 1 +min/max(T) = 617.01, 901.128 +GAMG: Solving for p, Initial residual = 0.0248955, Final residual = 0.000166248, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.34854e-06, global = 2.30076e-06, cumulative = 0.000567142 +GAMG: Solving for p, Initial residual = 0.000161282, Final residual = 3.05102e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.30711e-06, global = 2.30703e-06, cumulative = 0.000569449 +smoothSolver: Solving for epsilon, Initial residual = 0.00110013, Final residual = 1.85487e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00290768, Final residual = 4.79296e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097836 s +other Time = 0 s +rho Equations = 0.000221 s +U Equations = 0.001579 s +Y Equations = 0.00247213 s +E Equations = 0.000607 s +p Equations = 0.002282 s +calculate parcels = 25.4306 s +chemistry correctThermo = 0.002792 s +turbulence correct = 0.001019 s +combustion correct(in Y) = 0.0866069 s +percentage of chemistry = 88.5225 % +percentage of rho/U/Y/E = 4.98705 % +========Time details of each equation======= +rhoEqn Time = 0.000373 s +rhoEqn assamble = 0.000285 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001577 s +UEqn assamble = 0.00088 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000697 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001709 s +YEqn assamble = 0.00065 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000118 s +YEqn correct boundary = 0 s +EEqn Time = 0.000451 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 50.78 s ClockTime = 51 s +Courant Number mean: 0.000470435 max: 0.0184395 +Time = 0.00072 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 57 new parcels + +Cloud: sprayCloud + Current number of parcels = 12164 + Current mass in system = 1.12811e-09 + Linear momentum = (2.82271e-11 -9.97796e-09 0) + |Linear momentum| = 9.978e-09 + Linear kinetic energy = 4.66781e-08 + model1: + number of parcels added = 12174 + mass introduced = 1.15297e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.135, 515.286 + Mass transfer phase change = 2.48538e-11 + D10, D32, Dmax (mu) = 49.3872, 80.9817, 149.744 + Liquid penetration 95% mass (m) = 0.00561659 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00354392, Final residual = 5.72285e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0156036, Final residual = 3.84943e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00218549, Final residual = 1.34229e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00253361, Final residual = 1.21379e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0027856, Final residual = 1.61903e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00278561, Final residual = 1.62033e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196829, Final residual = 9.74184e-08, No Iterations 1 +min/max(T) = 616.769, 902.243 +GAMG: Solving for p, Initial residual = 0.0250199, Final residual = 0.000131696, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.35869e-06, global = 2.32248e-06, cumulative = 0.000571772 +GAMG: Solving for p, Initial residual = 0.000126628, Final residual = 9.66202e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.32804e-06, global = 2.32778e-06, cumulative = 0.0005741 +smoothSolver: Solving for epsilon, Initial residual = 0.00109716, Final residual = 1.84524e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00289017, Final residual = 4.75462e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.109258 s +other Time = 0 s +rho Equations = 0.000219 s +U Equations = 0.001591 s +Y Equations = 0.00265951 s +E Equations = 0.000616 s +p Equations = 0.002146 s +calculate parcels = 25.6402 s +chemistry correctThermo = 0.002769 s +turbulence correct = 0.001048 s +combustion correct(in Y) = 0.0979795 s +percentage of chemistry = 89.6772 % +percentage of rho/U/Y/E = 4.65459 % +========Time details of each equation======= +rhoEqn Time = 0.00037 s +rhoEqn assamble = 0.000284 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001589 s +UEqn assamble = 0.000897 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000692 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001592 s +YEqn assamble = 0.000688 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -2.5e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.00046 s +EEqn assamble = 0.000344 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 51.09 s ClockTime = 52 s +Courant Number mean: 0.000477697 max: 0.0184091 +Time = 0.0007225 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 43 new parcels + +Cloud: sprayCloud + Current number of parcels = 12206 + Current mass in system = 1.13089e-09 + Linear momentum = (2.84561e-11 -9.98952e-09 0) + |Linear momentum| = 9.98956e-09 + Linear kinetic energy = 4.66691e-08 + model1: + number of parcels added = 12217 + mass introduced = 1.15595e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.131, 515.475 + Mass transfer phase change = 2.50564e-11 + D10, D32, Dmax (mu) = 51.082, 81.0391, 149.678 + Liquid penetration 95% mass (m) = 0.0056332 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00344445, Final residual = 5.58573e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0154081, Final residual = 3.80898e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00215999, Final residual = 1.29301e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0025287, Final residual = 1.21017e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00278246, Final residual = 1.61808e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00278247, Final residual = 1.61938e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196495, Final residual = 9.67208e-08, No Iterations 1 +min/max(T) = 616.524, 903.368 +GAMG: Solving for p, Initial residual = 0.0252344, Final residual = 0.000126465, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.36892e-06, global = 2.33089e-06, cumulative = 0.000576431 +GAMG: Solving for p, Initial residual = 0.000122661, Final residual = 1.70292e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.33576e-06, global = 2.33571e-06, cumulative = 0.000578766 +smoothSolver: Solving for epsilon, Initial residual = 0.00109425, Final residual = 1.83656e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00287438, Final residual = 4.72352e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.088577 s +other Time = 0 s +rho Equations = 0.000147 s +U Equations = 0.000967 s +Y Equations = 0.00237771 s +E Equations = 0.000611 s +p Equations = 0.002216 s +calculate parcels = 25.8462 s +chemistry correctThermo = 0.002842 s +turbulence correct = 0.000985 s +combustion correct(in Y) = 0.0782543 s +percentage of chemistry = 88.3461 % +percentage of rho/U/Y/E = 4.6318 % +========Time details of each equation======= +rhoEqn Time = 0.000291 s +rhoEqn assamble = 0.000231 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000967 s +UEqn assamble = 0.000608 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000359 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001832 s +YEqn assamble = 0.000639 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000238 s +YEqn correct boundary = 0 s +EEqn Time = 0.000458 s +EEqn assamble = 0.000329 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000129 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 51.39 s ClockTime = 52 s +Courant Number mean: 0.000484935 max: 0.0183934 +Time = 0.000725 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 12257 + Current mass in system = 1.13421e-09 + Linear momentum = (2.73214e-11 -1.00066e-08 0) + |Linear momentum| = 1.00067e-08 + Linear kinetic energy = 4.66881e-08 + model1: + number of parcels added = 12268 + mass introduced = 1.15947e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.136, 515.659 + Mass transfer phase change = 2.52586e-11 + D10, D32, Dmax (mu) = 51.0894, 81.0637, 149.928 + Liquid penetration 95% mass (m) = 0.00564832 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00335469, Final residual = 5.32233e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0154192, Final residual = 3.80625e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00217666, Final residual = 1.29451e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00251908, Final residual = 1.18937e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00277904, Final residual = 1.61883e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00277905, Final residual = 1.6201e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196116, Final residual = 9.49464e-08, No Iterations 1 +min/max(T) = 616.282, 904.503 +GAMG: Solving for p, Initial residual = 0.0256673, Final residual = 0.00014375, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.36945e-06, global = 2.32678e-06, cumulative = 0.000581093 +GAMG: Solving for p, Initial residual = 0.00014013, Final residual = 9.21738e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.33123e-06, global = 2.33094e-06, cumulative = 0.000583424 +smoothSolver: Solving for epsilon, Initial residual = 0.00109136, Final residual = 1.82803e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00285914, Final residual = 4.69237e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.096084 s +other Time = 1e-06 s +rho Equations = 0.000168 s +U Equations = 0.001154 s +Y Equations = 0.0023931 s +E Equations = 0.000623 s +p Equations = 0.002078 s +calculate parcels = 26.0621 s +chemistry correctThermo = 0.002807 s +turbulence correct = 0.00104 s +combustion correct(in Y) = 0.0856169 s +percentage of chemistry = 89.1063 % +percentage of rho/U/Y/E = 4.5149 % +========Time details of each equation======= +rhoEqn Time = 0.000318 s +rhoEqn assamble = 0.000253 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001153 s +UEqn assamble = 0.000709 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000444 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001755 s +YEqn assamble = 0.00061 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00022 s +YEqn correct boundary = 0 s +EEqn Time = 0.000456 s +EEqn assamble = 0.000342 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 51.7 s ClockTime = 52 s +Courant Number mean: 0.000492112 max: 0.0183192 +Time = 0.0007275 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 40 new parcels + +Cloud: sprayCloud + Current number of parcels = 12296 + Current mass in system = 1.13677e-09 + Linear momentum = (2.74879e-11 -1.00159e-08 0) + |Linear momentum| = 1.0016e-08 + Linear kinetic energy = 4.66676e-08 + model1: + number of parcels added = 12308 + mass introduced = 1.16223e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.156, 515.835 + Mass transfer phase change = 2.54627e-11 + D10, D32, Dmax (mu) = 51.8605, 81.0921, 149.901 + Liquid penetration 95% mass (m) = 0.00566331 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00332036, Final residual = 5.26663e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0154762, Final residual = 3.82817e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00217464, Final residual = 1.32481e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00251922, Final residual = 1.19905e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00277571, Final residual = 1.61808e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00277572, Final residual = 1.61935e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196171, Final residual = 9.61156e-08, No Iterations 1 +min/max(T) = 616.052, 905.65 +GAMG: Solving for p, Initial residual = 0.0258131, Final residual = 0.000133895, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.38419e-06, global = 2.3475e-06, cumulative = 0.000585771 +GAMG: Solving for p, Initial residual = 0.000129014, Final residual = 1.58125e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.35205e-06, global = 2.35201e-06, cumulative = 0.000588123 +smoothSolver: Solving for epsilon, Initial residual = 0.00108798, Final residual = 1.81806e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00284345, Final residual = 4.65893e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.081139 s +other Time = 1e-06 s +rho Equations = 0.000138 s +U Equations = 0.000929 s +Y Equations = 0.00209994 s +E Equations = 0.000552 s +p Equations = 0.00193 s +calculate parcels = 26.2757 s +chemistry correctThermo = 0.001995 s +turbulence correct = 0.000868 s +combustion correct(in Y) = 0.0724601 s +percentage of chemistry = 89.3036 % +percentage of rho/U/Y/E = 4.58342 % +========Time details of each equation======= +rhoEqn Time = 0.000271 s +rhoEqn assamble = 0.000216 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000929 s +UEqn assamble = 0.000575 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000354 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001551 s +YEqn assamble = 0.000566 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000146 s +YEqn correct boundary = 0 s +EEqn Time = 0.000429 s +EEqn assamble = 0.000289 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00014 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 52 s ClockTime = 52 s +Courant Number mean: 0.000499289 max: 0.0182745 +Time = 0.00073 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 55 new parcels + +Cloud: sprayCloud + Current number of parcels = 12351 + Current mass in system = 1.14033e-09 + Linear momentum = (2.77958e-11 -1.00355e-08 0) + |Linear momentum| = 1.00355e-08 + Linear kinetic energy = 4.66996e-08 + model1: + number of parcels added = 12363 + mass introduced = 1.166e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.137, 516.006 + Mass transfer phase change = 2.56666e-11 + D10, D32, Dmax (mu) = 51.8614, 81.1238, 149.848 + Liquid penetration 95% mass (m) = 0.00567929 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00333159, Final residual = 5.25386e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0154842, Final residual = 3.82307e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0021554, Final residual = 1.25789e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00251111, Final residual = 1.19375e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00277255, Final residual = 1.61826e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00277256, Final residual = 1.61952e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196051, Final residual = 9.60111e-08, No Iterations 1 +min/max(T) = 615.831, 906.806 +GAMG: Solving for p, Initial residual = 0.0260523, Final residual = 0.000125396, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.38268e-06, global = 2.34617e-06, cumulative = 0.00059047 +GAMG: Solving for p, Initial residual = 0.00012043, Final residual = 1.46486e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.34969e-06, global = 2.34965e-06, cumulative = 0.000592819 +smoothSolver: Solving for epsilon, Initial residual = 0.00108502, Final residual = 1.80879e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00282864, Final residual = 4.6287e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.068856 s +other Time = 1e-06 s +rho Equations = 0.000165 s +U Equations = 0.000958 s +Y Equations = 0.00250711 s +E Equations = 0.000553 s +p Equations = 0.001906 s +calculate parcels = 26.428 s +chemistry correctThermo = 0.001932 s +turbulence correct = 0.000837 s +combustion correct(in Y) = 0.0598189 s +percentage of chemistry = 86.8754 % +percentage of rho/U/Y/E = 6.07515 % +========Time details of each equation======= +rhoEqn Time = 0.000288 s +rhoEqn assamble = 0.000231 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000958 s +UEqn assamble = 0.000601 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000357 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001946 s +YEqn assamble = 0.000783 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000228 s +YEqn correct boundary = 0 s +EEqn Time = 0.000402 s +EEqn assamble = 0.000307 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 52.22 s ClockTime = 53 s +Courant Number mean: 0.000506471 max: 0.0182252 +Time = 0.0007325 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 12395 + Current mass in system = 1.14315e-09 + Linear momentum = (2.76714e-11 -1.00474e-08 0) + |Linear momentum| = 1.00474e-08 + Linear kinetic energy = 4.66928e-08 + model1: + number of parcels added = 12407 + mass introduced = 1.16902e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.142, 516.169 + Mass transfer phase change = 2.58712e-11 + D10, D32, Dmax (mu) = 51.8871, 81.16, 149.77 + Liquid penetration 95% mass (m) = 0.00569475 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0032267, Final residual = 5.08786e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0154844, Final residual = 3.84185e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00214594, Final residual = 1.20504e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00250741, Final residual = 1.19084e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00276985, Final residual = 1.61691e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00276987, Final residual = 1.61817e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196053, Final residual = 9.6301e-08, No Iterations 1 +min/max(T) = 615.62, 907.973 +GAMG: Solving for p, Initial residual = 0.02639, Final residual = 0.000123163, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.39076e-06, global = 2.35723e-06, cumulative = 0.000595177 +GAMG: Solving for p, Initial residual = 0.000120664, Final residual = 9.51477e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.35896e-06, global = 2.35871e-06, cumulative = 0.000597535 +smoothSolver: Solving for epsilon, Initial residual = 0.00108163, Final residual = 1.79922e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00281388, Final residual = 4.59959e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092779 s +other Time = 0 s +rho Equations = 0.000154 s +U Equations = 0.000965 s +Y Equations = 0.00237909 s +E Equations = 0.000604 s +p Equations = 0.002014 s +calculate parcels = 26.6047 s +chemistry correctThermo = 0.002806 s +turbulence correct = 0.000986 s +combustion correct(in Y) = 0.0826889 s +percentage of chemistry = 89.1246 % +percentage of rho/U/Y/E = 4.42136 % +========Time details of each equation======= +rhoEqn Time = 0.000296 s +rhoEqn assamble = 0.000236 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000964 s +UEqn assamble = 0.000581 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000383 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00181 s +YEqn assamble = 0.000645 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000218 s +YEqn correct boundary = 0 s +EEqn Time = 0.000446 s +EEqn assamble = 0.000331 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 52.49 s ClockTime = 53 s +Courant Number mean: 0.000513688 max: 0.0181868 +Time = 0.000735 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 12441 + Current mass in system = 1.14608e-09 + Linear momentum = (2.83312e-11 -1.00606e-08 0) + |Linear momentum| = 1.00607e-08 + Linear kinetic energy = 4.66926e-08 + model1: + number of parcels added = 12453 + mass introduced = 1.17216e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.144, 516.325 + Mass transfer phase change = 2.60767e-11 + D10, D32, Dmax (mu) = 51.9135, 81.2049, 149.672 + Liquid penetration 95% mass (m) = 0.00571216 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00341796, Final residual = 5.32125e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.015428, Final residual = 3.8297e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0021437, Final residual = 1.18684e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0025036, Final residual = 1.19501e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00276673, Final residual = 1.61557e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00276674, Final residual = 1.61682e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196228, Final residual = 9.74535e-08, No Iterations 1 +min/max(T) = 615.418, 909.15 +GAMG: Solving for p, Initial residual = 0.026757, Final residual = 0.00012276, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.40015e-06, global = 2.36548e-06, cumulative = 0.000599901 +GAMG: Solving for p, Initial residual = 0.000118655, Final residual = 9.15736e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.3683e-06, global = 2.36803e-06, cumulative = 0.000602269 +smoothSolver: Solving for epsilon, Initial residual = 0.00107774, Final residual = 1.78917e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00279866, Final residual = 4.57101e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.093084 s +other Time = 1e-06 s +rho Equations = 0.000149 s +U Equations = 0.000935 s +Y Equations = 0.00227246 s +E Equations = 0.000606 s +p Equations = 0.002082 s +calculate parcels = 26.7997 s +chemistry correctThermo = 0.002841 s +turbulence correct = 0.00101 s +combustion correct(in Y) = 0.0829955 s +percentage of chemistry = 89.162 % +percentage of rho/U/Y/E = 4.25686 % +========Time details of each equation======= +rhoEqn Time = 0.000297 s +rhoEqn assamble = 0.000233 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000932 s +UEqn assamble = 0.000571 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000361 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001701 s +YEqn assamble = 0.000624 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00018 s +YEqn correct boundary = 0 s +EEqn Time = 0.000448 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 52.78 s ClockTime = 53 s +Courant Number mean: 0.000520917 max: 0.0181656 +Time = 0.0007375 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 12492 + Current mass in system = 1.14934e-09 + Linear momentum = (2.81632e-11 -1.00771e-08 0) + |Linear momentum| = 1.00771e-08 + Linear kinetic energy = 4.67092e-08 + model1: + number of parcels added = 12504 + mass introduced = 1.17563e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.151, 516.48 + Mass transfer phase change = 2.6283e-11 + D10, D32, Dmax (mu) = 51.6678, 81.2328, 149.738 + Liquid penetration 95% mass (m) = 0.00572858 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00378599, Final residual = 5.7291e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0153424, Final residual = 3.79402e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00213597, Final residual = 1.15391e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00250044, Final residual = 1.19971e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00276394, Final residual = 1.61362e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00276395, Final residual = 1.61487e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196676, Final residual = 9.918e-08, No Iterations 1 +min/max(T) = 615.212, 910.338 +GAMG: Solving for p, Initial residual = 0.0272581, Final residual = 0.000120539, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.40943e-06, global = 2.37747e-06, cumulative = 0.000604646 +GAMG: Solving for p, Initial residual = 0.000118058, Final residual = 1.52137e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.37856e-06, global = 2.37852e-06, cumulative = 0.000607025 +smoothSolver: Solving for epsilon, Initial residual = 0.00107397, Final residual = 1.7788e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00278337, Final residual = 4.54191e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094014 s +other Time = 1e-06 s +rho Equations = 0.000205 s +U Equations = 0.001125 s +Y Equations = 0.00248111 s +E Equations = 0.000597 s +p Equations = 0.002177 s +calculate parcels = 27.0087 s +chemistry correctThermo = 0.0028 s +turbulence correct = 0.000982 s +combustion correct(in Y) = 0.0834239 s +percentage of chemistry = 88.7356 % +percentage of rho/U/Y/E = 4.68878 % +========Time details of each equation======= +rhoEqn Time = 0.000345 s +rhoEqn assamble = 0.000277 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001125 s +UEqn assamble = 0.000689 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000436 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001832 s +YEqn assamble = 0.000664 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00018 s +YEqn correct boundary = 0 s +EEqn Time = 0.000442 s +EEqn assamble = 0.000329 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 53.08 s ClockTime = 54 s +Courant Number mean: 0.000528262 max: 0.0181561 +Time = 0.00074 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 12536 + Current mass in system = 1.15213e-09 + Linear momentum = (2.84471e-11 -1.00887e-08 0) + |Linear momentum| = 1.00887e-08 + Linear kinetic energy = 4.67014e-08 + model1: + number of parcels added = 12548 + mass introduced = 1.17862e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.149, 516.632 + Mass transfer phase change = 2.64903e-11 + D10, D32, Dmax (mu) = 51.6786, 81.2638, 149.683 + Liquid penetration 95% mass (m) = 0.00574359 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00381793, Final residual = 5.87432e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0152239, Final residual = 3.75798e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00212634, Final residual = 1.14345e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00249688, Final residual = 1.20004e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00276111, Final residual = 1.61206e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00276112, Final residual = 1.61331e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196523, Final residual = 9.88926e-08, No Iterations 1 +min/max(T) = 615.02, 911.537 +GAMG: Solving for p, Initial residual = 0.0275471, Final residual = 0.000111708, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.41716e-06, global = 2.3871e-06, cumulative = 0.000609412 +GAMG: Solving for p, Initial residual = 0.000109185, Final residual = 9.6253e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.38891e-06, global = 2.38866e-06, cumulative = 0.000611801 +smoothSolver: Solving for epsilon, Initial residual = 0.00106988, Final residual = 1.76816e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00276763, Final residual = 4.51282e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095865 s +other Time = 0 s +rho Equations = 0.000172 s +U Equations = 0.001128 s +Y Equations = 0.00239948 s +E Equations = 0.000613 s +p Equations = 0.00209 s +calculate parcels = 27.2216 s +chemistry correctThermo = 0.002811 s +turbulence correct = 0.001006 s +combustion correct(in Y) = 0.0854465 s +percentage of chemistry = 89.1321 % +percentage of rho/U/Y/E = 4.49849 % +========Time details of each equation======= +rhoEqn Time = 0.000319 s +rhoEqn assamble = 0.000252 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001128 s +UEqn assamble = 0.000673 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000455 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001754 s +YEqn assamble = 0.00065 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000171 s +YEqn correct boundary = 0 s +EEqn Time = 0.000459 s +EEqn assamble = 0.000343 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 53.39 s ClockTime = 54 s +Courant Number mean: 0.000535715 max: 0.0181528 +Time = 0.0007425 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 63 new parcels + +Cloud: sprayCloud + Current number of parcels = 12599 + Current mass in system = 1.15618e-09 + Linear momentum = (2.7627e-11 -1.01131e-08 0) + |Linear momentum| = 1.01131e-08 + Linear kinetic energy = 4.67582e-08 + model1: + number of parcels added = 12611 + mass introduced = 1.18288e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.134, 516.78 + Mass transfer phase change = 2.66984e-11 + D10, D32, Dmax (mu) = 51.686, 81.3233, 149.688 + Liquid penetration 95% mass (m) = 0.00575768 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00384294, Final residual = 6.09573e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.015046, Final residual = 3.70821e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00212351, Final residual = 1.14214e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0024935, Final residual = 1.20307e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0027583, Final residual = 1.60994e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00275831, Final residual = 1.61118e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196471, Final residual = 9.89375e-08, No Iterations 1 +min/max(T) = 614.834, 912.746 +GAMG: Solving for p, Initial residual = 0.0279087, Final residual = 9.61146e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.42659e-06, global = 2.3969e-06, cumulative = 0.000614197 +GAMG: Solving for p, Initial residual = 9.30775e-05, Final residual = 6.19008e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.39943e-06, global = 2.39923e-06, cumulative = 0.000616597 +smoothSolver: Solving for epsilon, Initial residual = 0.00106596, Final residual = 1.75757e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00275214, Final residual = 4.48425e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094813 s +other Time = 0 s +rho Equations = 0.00018 s +U Equations = 0.001144 s +Y Equations = 0.00231484 s +E Equations = 0.00049 s +p Equations = 0.002127 s +calculate parcels = 27.4307 s +chemistry correctThermo = 0.002612 s +turbulence correct = 0.001274 s +combustion correct(in Y) = 0.0844572 s +percentage of chemistry = 89.0776 % +percentage of rho/U/Y/E = 4.35472 % +========Time details of each equation======= +rhoEqn Time = 0.000348 s +rhoEqn assamble = 0.000275 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001143 s +UEqn assamble = 0.000697 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000446 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001677 s +YEqn assamble = 0.000654 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000141 s +YEqn correct boundary = 0 s +EEqn Time = 0.000371 s +EEqn assamble = 0.000276 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 53.69 s ClockTime = 54 s +Courant Number mean: 0.000543289 max: 0.0181422 +Time = 0.000745 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 12645 + Current mass in system = 1.15909e-09 + Linear momentum = (2.77737e-11 -1.0126e-08 0) + |Linear momentum| = 1.0126e-08 + Linear kinetic energy = 4.67566e-08 + model1: + number of parcels added = 12657 + mass introduced = 1.186e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.138, 516.922 + Mass transfer phase change = 2.69077e-11 + D10, D32, Dmax (mu) = 50.3034, 81.2926, 149.694 + Liquid penetration 95% mass (m) = 0.00577369 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00383387, Final residual = 6.21779e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0148298, Final residual = 3.65453e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00211866, Final residual = 1.14641e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00249116, Final residual = 1.208e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00275546, Final residual = 1.60724e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00275548, Final residual = 1.60847e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00197343, Final residual = 1.00852e-07, No Iterations 1 +min/max(T) = 614.66, 913.966 +GAMG: Solving for p, Initial residual = 0.0284571, Final residual = 0.00014406, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.45174e-06, global = 2.40637e-06, cumulative = 0.000619003 +GAMG: Solving for p, Initial residual = 0.000141153, Final residual = 3.03002e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.41283e-06, global = 2.41275e-06, cumulative = 0.000621416 +smoothSolver: Solving for epsilon, Initial residual = 0.00106212, Final residual = 1.74648e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00273772, Final residual = 4.45519e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097062 s +other Time = 0 s +rho Equations = 0.000195 s +U Equations = 0.001112 s +Y Equations = 0.00237685 s +E Equations = 0.000598 s +p Equations = 0.00226 s +calculate parcels = 27.639 s +chemistry correctThermo = 0.002761 s +turbulence correct = 0.000953 s +combustion correct(in Y) = 0.0866111 s +percentage of chemistry = 89.2328 % +percentage of rho/U/Y/E = 4.41146 % +========Time details of each equation======= +rhoEqn Time = 0.00034 s +rhoEqn assamble = 0.000268 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00111 s +UEqn assamble = 0.00068 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00043 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001734 s +YEqn assamble = 0.000607 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000206 s +YEqn correct boundary = 0 s +EEqn Time = 0.000444 s +EEqn assamble = 0.00033 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 54 s ClockTime = 54 s +Courant Number mean: 0.000551108 max: 0.0181365 +Time = 0.0007475 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 12695 + Current mass in system = 1.16226e-09 + Linear momentum = (2.80394e-11 -1.01415e-08 0) + |Linear momentum| = 1.01415e-08 + Linear kinetic energy = 4.67682e-08 + model1: + number of parcels added = 12707 + mass introduced = 1.18938e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.144, 517.048 + Mass transfer phase change = 2.71181e-11 + D10, D32, Dmax (mu) = 50.3007, 81.3248, 149.699 + Liquid penetration 95% mass (m) = 0.00578747 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00380678, Final residual = 6.2911e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0145958, Final residual = 3.58807e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00211215, Final residual = 1.147e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00248803, Final residual = 1.21276e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00275281, Final residual = 1.60565e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00275282, Final residual = 1.60689e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196951, Final residual = 1.00909e-07, No Iterations 1 +min/max(T) = 614.48, 915.197 +GAMG: Solving for p, Initial residual = 0.0290876, Final residual = 0.000169179, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.46709e-06, global = 2.42067e-06, cumulative = 0.000623836 +GAMG: Solving for p, Initial residual = 0.000166279, Final residual = 2.43092e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.42442e-06, global = 2.42435e-06, cumulative = 0.000626261 +smoothSolver: Solving for epsilon, Initial residual = 0.00105774, Final residual = 1.73551e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0027222, Final residual = 4.42524e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.088112 s +other Time = 1e-06 s +rho Equations = 0.000187 s +U Equations = 0.001118 s +Y Equations = 0.00244079 s +E Equations = 0.000617 s +p Equations = 0.00221 s +calculate parcels = 27.8601 s +chemistry correctThermo = 0.002757 s +turbulence correct = 0.000998 s +combustion correct(in Y) = 0.0775832 s +percentage of chemistry = 88.0507 % +percentage of rho/U/Y/E = 4.95141 % +========Time details of each equation======= +rhoEqn Time = 0.000332 s +rhoEqn assamble = 0.000247 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001117 s +UEqn assamble = 0.000682 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000435 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001785 s +YEqn assamble = 0.000655 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000206 s +YEqn correct boundary = 0 s +EEqn Time = 0.000458 s +EEqn assamble = 0.000341 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 54.31 s ClockTime = 55 s +Courant Number mean: 0.00055901 max: 0.0181164 +Time = 0.00075 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 52 new parcels + +Cloud: sprayCloud + Current number of parcels = 12747 + Current mass in system = 1.16556e-09 + Linear momentum = (2.80332e-11 -1.01582e-08 0) + |Linear momentum| = 1.01582e-08 + Linear kinetic energy = 4.67861e-08 + model1: + number of parcels added = 12759 + mass introduced = 1.19289e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.156, 517.166 + Mass transfer phase change = 2.73295e-11 + D10, D32, Dmax (mu) = 50.262, 81.3475, 149.705 + Liquid penetration 95% mass (m) = 0.0058029 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00367342, Final residual = 6.28977e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0142776, Final residual = 3.50319e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0021079, Final residual = 1.18168e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00248519, Final residual = 1.22665e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00274992, Final residual = 1.60398e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00274993, Final residual = 1.60521e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196832, Final residual = 1.02278e-07, No Iterations 1 +min/max(T) = 614.296, 916.44 +GAMG: Solving for p, Initial residual = 0.0294168, Final residual = 0.000157438, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.47991e-06, global = 2.43083e-06, cumulative = 0.000628692 +GAMG: Solving for p, Initial residual = 0.000152473, Final residual = 2.49596e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.43706e-06, global = 2.43698e-06, cumulative = 0.000631129 +smoothSolver: Solving for epsilon, Initial residual = 0.00105346, Final residual = 1.72466e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00270707, Final residual = 4.3958e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.070144 s +other Time = 1e-06 s +rho Equations = 0.000219 s +U Equations = 0.001321 s +Y Equations = 0.00225077 s +E Equations = 0.00052 s +p Equations = 0.001774 s +calculate parcels = 28.0379 s +chemistry correctThermo = 0.001984 s +turbulence correct = 0.000967 s +combustion correct(in Y) = 0.0608782 s +percentage of chemistry = 86.7904 % +percentage of rho/U/Y/E = 6.1456 % +========Time details of each equation======= +rhoEqn Time = 0.000338 s +rhoEqn assamble = 0.000269 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00132 s +UEqn assamble = 0.000831 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000489 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001524 s +YEqn assamble = 0.00056 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 3.4e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000394 s +EEqn assamble = 0.000297 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.7e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 54.55 s ClockTime = 55 s +Courant Number mean: 0.000566943 max: 0.0181072 +Time = 0.0007525 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 12795 + Current mass in system = 1.16859e-09 + Linear momentum = (2.77779e-11 -1.01722e-08 0) + |Linear momentum| = 1.01723e-08 + Linear kinetic energy = 4.67906e-08 + model1: + number of parcels added = 12807 + mass introduced = 1.19613e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.133, 517.284 + Mass transfer phase change = 2.7542e-11 + D10, D32, Dmax (mu) = 50.2861, 81.4036, 149.71 + Liquid penetration 95% mass (m) = 0.00582029 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00371932, Final residual = 6.20736e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0139525, Final residual = 3.41829e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00210052, Final residual = 1.2058e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00248248, Final residual = 1.22901e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00274789, Final residual = 1.60315e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0027479, Final residual = 1.60438e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196919, Final residual = 1.03157e-07, No Iterations 1 +min/max(T) = 614.116, 917.695 +GAMG: Solving for p, Initial residual = 0.0300962, Final residual = 0.000149635, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.48926e-06, global = 2.44366e-06, cumulative = 0.000633572 +GAMG: Solving for p, Initial residual = 0.000145562, Final residual = 1.83021e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.44859e-06, global = 2.44854e-06, cumulative = 0.000636021 +smoothSolver: Solving for epsilon, Initial residual = 0.00104944, Final residual = 1.71438e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00269253, Final residual = 4.36824e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.070869 s +other Time = 1e-06 s +rho Equations = 0.000274 s +U Equations = 0.001312 s +Y Equations = 0.00213211 s +E Equations = 0.00057 s +p Equations = 0.002056 s +calculate parcels = 28.1969 s +chemistry correctThermo = 0.001917 s +turbulence correct = 0.000814 s +combustion correct(in Y) = 0.0615709 s +percentage of chemistry = 86.8799 % +percentage of rho/U/Y/E = 6.05076 % +========Time details of each equation======= +rhoEqn Time = 0.000398 s +rhoEqn assamble = 0.000322 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001309 s +UEqn assamble = 0.000831 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000478 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001436 s +YEqn assamble = 0.00056 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 6e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000451 s +EEqn assamble = 0.000354 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.7e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 54.78 s ClockTime = 55 s +Courant Number mean: 0.00057484 max: 0.0181042 +Time = 0.000755 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 56 new parcels + +Cloud: sprayCloud + Current number of parcels = 12851 + Current mass in system = 1.17215e-09 + Linear momentum = (2.84716e-11 -1.01916e-08 0) + |Linear momentum| = 1.01916e-08 + Linear kinetic energy = 4.68221e-08 + model1: + number of parcels added = 12863 + mass introduced = 1.1999e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.133, 517.401 + Mass transfer phase change = 2.77554e-11 + D10, D32, Dmax (mu) = 50.3115, 81.451, 149.716 + Liquid penetration 95% mass (m) = 0.00583603 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00368299, Final residual = 6.02614e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0136506, Final residual = 3.36674e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00209251, Final residual = 1.20665e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00247948, Final residual = 1.22963e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00274524, Final residual = 1.60399e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00274525, Final residual = 1.60522e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196426, Final residual = 1.02678e-07, No Iterations 1 +min/max(T) = 613.959, 918.964 +GAMG: Solving for p, Initial residual = 0.0307097, Final residual = 0.000147132, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.50345e-06, global = 2.4566e-06, cumulative = 0.000638477 +GAMG: Solving for p, Initial residual = 0.000142682, Final residual = 1.67638e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.46038e-06, global = 2.46032e-06, cumulative = 0.000640938 +smoothSolver: Solving for epsilon, Initial residual = 0.00104551, Final residual = 1.70401e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0026782, Final residual = 4.34133e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.096325 s +other Time = 0 s +rho Equations = 0.000151 s +U Equations = 0.000981 s +Y Equations = 0.00233778 s +E Equations = 0.000611 s +p Equations = 0.002206 s +calculate parcels = 28.4267 s +chemistry correctThermo = 0.00281 s +turbulence correct = 0.001049 s +combustion correct(in Y) = 0.0860022 s +percentage of chemistry = 89.2834 % +percentage of rho/U/Y/E = 4.23647 % +========Time details of each equation======= +rhoEqn Time = 0.000296 s +rhoEqn assamble = 0.000231 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00098 s +UEqn assamble = 0.000603 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000377 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001776 s +YEqn assamble = 0.000635 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000228 s +YEqn correct boundary = 0 s +EEqn Time = 0.000452 s +EEqn assamble = 0.000338 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 55.11 s ClockTime = 56 s +Courant Number mean: 0.000582779 max: 0.0180988 +Time = 0.0007575 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 12902 + Current mass in system = 1.17537e-09 + Linear momentum = (2.84184e-11 -1.02076e-08 0) + |Linear momentum| = 1.02076e-08 + Linear kinetic energy = 4.68371e-08 + model1: + number of parcels added = 12914 + mass introduced = 1.20334e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.151, 517.514 + Mass transfer phase change = 2.797e-11 + D10, D32, Dmax (mu) = 50.1603, 81.4722, 149.722 + Liquid penetration 95% mass (m) = 0.00585177 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00363719, Final residual = 6.02364e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0133419, Final residual = 3.31345e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0020917, Final residual = 1.20492e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00247759, Final residual = 1.22968e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00274381, Final residual = 1.60644e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00274382, Final residual = 1.60768e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196169, Final residual = 1.02131e-07, No Iterations 1 +min/max(T) = 613.828, 920.244 +GAMG: Solving for p, Initial residual = 0.0314866, Final residual = 0.000177841, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.52537e-06, global = 2.46792e-06, cumulative = 0.000643406 +GAMG: Solving for p, Initial residual = 0.000172851, Final residual = 2.82619e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.47367e-06, global = 2.47359e-06, cumulative = 0.000645879 +smoothSolver: Solving for epsilon, Initial residual = 0.00104151, Final residual = 1.69307e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.002664, Final residual = 4.31418e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097294 s +other Time = 1e-06 s +rho Equations = 0.000171 s +U Equations = 0.001148 s +Y Equations = 0.00239077 s +E Equations = 0.000606 s +p Equations = 0.002206 s +calculate parcels = 28.653 s +chemistry correctThermo = 0.002796 s +turbulence correct = 0.001 s +combustion correct(in Y) = 0.0867792 s +percentage of chemistry = 89.1928 % +percentage of rho/U/Y/E = 4.4358 % +========Time details of each equation======= +rhoEqn Time = 0.000318 s +rhoEqn assamble = 0.000252 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001147 s +UEqn assamble = 0.000706 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000441 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001736 s +YEqn assamble = 0.000665 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00017 s +YEqn correct boundary = 0 s +EEqn Time = 0.000449 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 55.43 s ClockTime = 56 s +Courant Number mean: 0.000590819 max: 0.0180814 +Time = 0.00076 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 45 new parcels + +Cloud: sprayCloud + Current number of parcels = 12947 + Current mass in system = 1.17819e-09 + Linear momentum = (2.91139e-11 -1.02197e-08 0) + |Linear momentum| = 1.02197e-08 + Linear kinetic energy = 4.68321e-08 + model1: + number of parcels added = 12959 + mass introduced = 1.20638e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.135, 517.616 + Mass transfer phase change = 2.81857e-11 + D10, D32, Dmax (mu) = 50.1769, 81.4971, 149.727 + Liquid penetration 95% mass (m) = 0.00586738 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.003557, Final residual = 5.97396e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0130571, Final residual = 3.25711e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00208402, Final residual = 1.19548e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00247469, Final residual = 1.23351e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00274144, Final residual = 1.60838e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00274146, Final residual = 1.60962e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00195726, Final residual = 1.01455e-07, No Iterations 1 +min/max(T) = 613.719, 921.535 +GAMG: Solving for p, Initial residual = 0.0319716, Final residual = 0.000155981, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.52967e-06, global = 2.48127e-06, cumulative = 0.00064836 +GAMG: Solving for p, Initial residual = 0.000151658, Final residual = 1.81014e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.48547e-06, global = 2.48542e-06, cumulative = 0.000650846 +smoothSolver: Solving for epsilon, Initial residual = 0.00103704, Final residual = 1.68181e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00264964, Final residual = 4.28935e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.082493 s +other Time = 0 s +rho Equations = 0.000138 s +U Equations = 0.000986 s +Y Equations = 0.00234563 s +E Equations = 0.000599 s +p Equations = 0.002274 s +calculate parcels = 28.8679 s +chemistry correctThermo = 0.002771 s +turbulence correct = 0.001023 s +combustion correct(in Y) = 0.0721794 s +percentage of chemistry = 87.4976 % +percentage of rho/U/Y/E = 4.9321 % +========Time details of each equation======= +rhoEqn Time = 0.000287 s +rhoEqn assamble = 0.00023 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000985 s +UEqn assamble = 0.000597 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000388 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001778 s +YEqn assamble = 0.000665 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000222 s +YEqn correct boundary = 0 s +EEqn Time = 0.000444 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 55.73 s ClockTime = 56 s +Courant Number mean: 0.000598961 max: 0.0180654 +Time = 0.0007625 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 45 new parcels + +Cloud: sprayCloud + Current number of parcels = 12992 + Current mass in system = 1.181e-09 + Linear momentum = (2.98066e-11 -1.02316e-08 0) + |Linear momentum| = 1.02316e-08 + Linear kinetic energy = 4.68269e-08 + model1: + number of parcels added = 13004 + mass introduced = 1.2094e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.15, 517.71 + Mass transfer phase change = 2.84024e-11 + D10, D32, Dmax (mu) = 50.1589, 81.5119, 149.733 + Liquid penetration 95% mass (m) = 0.0058835 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00358643, Final residual = 5.93908e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0127704, Final residual = 3.19909e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00208044, Final residual = 1.19261e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00247277, Final residual = 1.23948e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00274, Final residual = 1.61017e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00274001, Final residual = 1.61141e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00195418, Final residual = 1.00744e-07, No Iterations 1 +min/max(T) = 613.63, 922.838 +GAMG: Solving for p, Initial residual = 0.0326268, Final residual = 0.000143572, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.53855e-06, global = 2.49435e-06, cumulative = 0.00065334 +GAMG: Solving for p, Initial residual = 0.000139659, Final residual = 1.33855e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.49823e-06, global = 2.49819e-06, cumulative = 0.000655838 +smoothSolver: Solving for epsilon, Initial residual = 0.00103229, Final residual = 1.67019e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00263497, Final residual = 4.26482e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.075217 s +other Time = 1e-06 s +rho Equations = 0.00014 s +U Equations = 0.000921 s +Y Equations = 0.00202525 s +E Equations = 0.000494 s +p Equations = 0.001814 s +calculate parcels = 29.0754 s +chemistry correctThermo = 0.002006 s +turbulence correct = 0.000811 s +combustion correct(in Y) = 0.0668377 s +percentage of chemistry = 88.8599 % +percentage of rho/U/Y/E = 4.7599 % +========Time details of each equation======= +rhoEqn Time = 0.000272 s +rhoEqn assamble = 0.000213 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000919 s +UEqn assamble = 0.00056 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000359 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001474 s +YEqn assamble = 0.000553 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000138 s +YEqn correct boundary = 0 s +EEqn Time = 0.000376 s +EEqn assamble = 0.000284 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 56.01 s ClockTime = 56 s +Courant Number mean: 0.000607234 max: 0.0180563 +Time = 0.000765 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 52 new parcels + +Cloud: sprayCloud + Current number of parcels = 13044 + Current mass in system = 1.18427e-09 + Linear momentum = (3.04053e-11 -1.02481e-08 0) + |Linear momentum| = 1.02481e-08 + Linear kinetic energy = 4.68448e-08 + model1: + number of parcels added = 13056 + mass introduced = 1.21289e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.138, 517.795 + Mass transfer phase change = 2.86202e-11 + D10, D32, Dmax (mu) = 50.1793, 81.5557, 149.739 + Liquid penetration 95% mass (m) = 0.00589848 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00379054, Final residual = 6.31182e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0125523, Final residual = 3.14464e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00207167, Final residual = 1.1714e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00247053, Final residual = 1.24184e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00273829, Final residual = 1.61192e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0027383, Final residual = 1.61316e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00195057, Final residual = 9.98639e-08, No Iterations 1 +min/max(T) = 613.562, 924.153 +GAMG: Solving for p, Initial residual = 0.0333787, Final residual = 0.000129789, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.54719e-06, global = 2.50645e-06, cumulative = 0.000658345 +GAMG: Solving for p, Initial residual = 0.000125613, Final residual = 8.2317e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.5106e-06, global = 2.51035e-06, cumulative = 0.000660855 +smoothSolver: Solving for epsilon, Initial residual = 0.00102755, Final residual = 1.65832e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0026205, Final residual = 4.24124e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.071875 s +other Time = 1e-06 s +rho Equations = 0.000144 s +U Equations = 0.000932 s +Y Equations = 0.00207369 s +E Equations = 0.000491 s +p Equations = 0.001632 s +calculate parcels = 29.2628 s +chemistry correctThermo = 0.002032 s +turbulence correct = 0.000863 s +combustion correct(in Y) = 0.0635393 s +percentage of chemistry = 88.4025 % +percentage of rho/U/Y/E = 5.0653 % +========Time details of each equation======= +rhoEqn Time = 0.00026 s +rhoEqn assamble = 0.000208 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000931 s +UEqn assamble = 0.000565 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000366 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001512 s +YEqn assamble = 0.000564 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000145 s +YEqn correct boundary = 0 s +EEqn Time = 0.000373 s +EEqn assamble = 0.00028 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 56.27 s ClockTime = 57 s +Courant Number mean: 0.000615603 max: 0.0180522 +Time = 0.0007675 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 45 new parcels + +Cloud: sprayCloud + Current number of parcels = 13089 + Current mass in system = 1.18706e-09 + Linear momentum = (3.02303e-11 -1.026e-08 0) + |Linear momentum| = 1.026e-08 + Linear kinetic energy = 4.68397e-08 + model1: + number of parcels added = 13101 + mass introduced = 1.2159e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.154, 517.872 + Mass transfer phase change = 2.8839e-11 + D10, D32, Dmax (mu) = 50.1972, 81.5937, 149.744 + Liquid penetration 95% mass (m) = 0.00591442 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00392976, Final residual = 6.51878e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0124317, Final residual = 3.12284e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00206907, Final residual = 1.16823e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00246826, Final residual = 1.24479e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00273708, Final residual = 1.61563e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0027371, Final residual = 1.61688e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00195122, Final residual = 9.92712e-08, No Iterations 1 +min/max(T) = 613.515, 925.481 +GAMG: Solving for p, Initial residual = 0.0343226, Final residual = 0.000150068, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.56274e-06, global = 2.51709e-06, cumulative = 0.000663372 +GAMG: Solving for p, Initial residual = 0.000146228, Final residual = 1.60524e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.52168e-06, global = 2.52163e-06, cumulative = 0.000665894 +smoothSolver: Solving for epsilon, Initial residual = 0.00102362, Final residual = 1.64629e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00260702, Final residual = 4.21799e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.08999 s +other Time = 1e-06 s +rho Equations = 0.000143 s +U Equations = 0.000949 s +Y Equations = 0.00234704 s +E Equations = 0.000629 s +p Equations = 0.001923 s +calculate parcels = 29.4803 s +chemistry correctThermo = 0.002026 s +turbulence correct = 0.001012 s +combustion correct(in Y) = 0.080793 s +percentage of chemistry = 89.7799 % +percentage of rho/U/Y/E = 4.52054 % +========Time details of each equation======= +rhoEqn Time = 0.000278 s +rhoEqn assamble = 0.000219 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000947 s +UEqn assamble = 0.000568 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000379 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00178 s +YEqn assamble = 0.000648 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000214 s +YEqn correct boundary = 0 s +EEqn Time = 0.000458 s +EEqn assamble = 0.000343 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 56.58 s ClockTime = 57 s +Courant Number mean: 0.000624041 max: 0.0180263 +Time = 0.00077 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 45 new parcels + +Cloud: sprayCloud + Current number of parcels = 13134 + Current mass in system = 1.18985e-09 + Linear momentum = (3.05599e-11 -1.02718e-08 0) + |Linear momentum| = 1.02718e-08 + Linear kinetic energy = 4.68345e-08 + model1: + number of parcels added = 13146 + mass introduced = 1.21891e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.138, 517.938 + Mass transfer phase change = 2.90588e-11 + D10, D32, Dmax (mu) = 50.2203, 81.6321, 149.75 + Liquid penetration 95% mass (m) = 0.00592908 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00396751, Final residual = 6.51477e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0123999, Final residual = 3.12869e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00206131, Final residual = 1.16252e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00246571, Final residual = 1.24622e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00273556, Final residual = 1.61908e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00273557, Final residual = 1.62033e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00194714, Final residual = 9.84281e-08, No Iterations 1 +min/max(T) = 613.487, 926.821 +GAMG: Solving for p, Initial residual = 0.0349356, Final residual = 0.000129142, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.57073e-06, global = 2.52913e-06, cumulative = 0.000668423 +GAMG: Solving for p, Initial residual = 0.000125193, Final residual = 1.59797e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.53305e-06, global = 2.533e-06, cumulative = 0.000670956 +smoothSolver: Solving for epsilon, Initial residual = 0.00102025, Final residual = 1.6342e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00259321, Final residual = 4.19378e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.086401 s +other Time = 0 s +rho Equations = 0.000165 s +U Equations = 0.001099 s +Y Equations = 0.00216357 s +E Equations = 0.000521 s +p Equations = 0.002005 s +calculate parcels = 29.7078 s +chemistry correctThermo = 0.001951 s +turbulence correct = 0.000863 s +combustion correct(in Y) = 0.0774504 s +percentage of chemistry = 89.6407 % +percentage of rho/U/Y/E = 4.57005 % +========Time details of each equation======= +rhoEqn Time = 0.000293 s +rhoEqn assamble = 0.000232 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001099 s +UEqn assamble = 0.000668 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000431 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001495 s +YEqn assamble = 0.000581 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 7.7e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000396 s +EEqn assamble = 0.000301 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 56.9 s ClockTime = 57 s +Courant Number mean: 0.000632609 max: 0.0180022 +Time = 0.0007725 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 13178 + Current mass in system = 1.19256e-09 + Linear momentum = (3.07267e-11 -1.02829e-08 0) + |Linear momentum| = 1.02829e-08 + Linear kinetic energy = 4.68259e-08 + model1: + number of parcels added = 13190 + mass introduced = 1.22184e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.141, 517.973 + Mass transfer phase change = 2.92795e-11 + D10, D32, Dmax (mu) = 50.2354, 81.6748, 149.755 + Liquid penetration 95% mass (m) = 0.00594395 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00404564, Final residual = 6.70662e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0123744, Final residual = 3.11727e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00205508, Final residual = 1.15927e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00246338, Final residual = 1.25023e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00273459, Final residual = 1.62247e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0027346, Final residual = 1.62373e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00194181, Final residual = 9.78657e-08, No Iterations 1 +min/max(T) = 613.479, 928.174 +GAMG: Solving for p, Initial residual = 0.0359093, Final residual = 0.000140355, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.58285e-06, global = 2.5395e-06, cumulative = 0.000673496 +GAMG: Solving for p, Initial residual = 0.000135893, Final residual = 1.40904e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.54416e-06, global = 2.54412e-06, cumulative = 0.00067604 +smoothSolver: Solving for epsilon, Initial residual = 0.00101698, Final residual = 1.62307e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00257875, Final residual = 4.16855e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.069795 s +other Time = 1e-06 s +rho Equations = 0.000206 s +U Equations = 0.00116 s +Y Equations = 0.00230292 s +E Equations = 0.000551 s +p Equations = 0.00218 s +calculate parcels = 29.8739 s +chemistry correctThermo = 0.001921 s +turbulence correct = 0.001126 s +combustion correct(in Y) = 0.0601161 s +percentage of chemistry = 86.1324 % +percentage of rho/U/Y/E = 6.04616 % +========Time details of each equation======= +rhoEqn Time = 0.000351 s +rhoEqn assamble = 0.000279 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001158 s +UEqn assamble = 0.000765 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000393 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00133 s +YEqn assamble = 0.000557 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -7.5e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000414 s +EEqn assamble = 0.000316 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 57.13 s ClockTime = 58 s +Courant Number mean: 0.000641272 max: 0.0179944 +Time = 0.000775 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 45 new parcels + +Cloud: sprayCloud + Current number of parcels = 13223 + Current mass in system = 1.19532e-09 + Linear momentum = (3.02637e-11 -1.02945e-08 0) + |Linear momentum| = 1.02946e-08 + Linear kinetic energy = 4.68205e-08 + model1: + number of parcels added = 13235 + mass introduced = 1.22482e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.146, 520.535 + Mass transfer phase change = 2.95012e-11 + D10, D32, Dmax (mu) = 50.2568, 81.7235, 149.761 + Liquid penetration 95% mass (m) = 0.00596021 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00430419, Final residual = 7.19911e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.012354, Final residual = 3.10181e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00205091, Final residual = 1.15602e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00246155, Final residual = 1.25573e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00273407, Final residual = 1.62557e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00273408, Final residual = 1.62683e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00193979, Final residual = 9.75615e-08, No Iterations 1 +min/max(T) = 613.498, 929.539 +GAMG: Solving for p, Initial residual = 0.0367863, Final residual = 0.000120237, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.58814e-06, global = 2.55213e-06, cumulative = 0.000678592 +GAMG: Solving for p, Initial residual = 0.000117488, Final residual = 1.47056e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.55561e-06, global = 2.55557e-06, cumulative = 0.000681147 +smoothSolver: Solving for epsilon, Initial residual = 0.00101526, Final residual = 1.61171e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00256483, Final residual = 4.14412e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.099435 s +other Time = 0 s +rho Equations = 0.00017 s +U Equations = 0.001121 s +Y Equations = 0.00370418 s +E Equations = 0.000607 s +p Equations = 0.002319 s +calculate parcels = 30.0721 s +chemistry correctThermo = 0.002792 s +turbulence correct = 0.001004 s +combustion correct(in Y) = 0.0875178 s +percentage of chemistry = 88.0151 % +percentage of rho/U/Y/E = 5.63401 % +========Time details of each equation======= +rhoEqn Time = 0.000317 s +rhoEqn assamble = 0.000252 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001119 s +UEqn assamble = 0.000692 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000427 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.003079 s +YEqn assamble = 0.001 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000504 s +YEqn correct boundary = 0 s +EEqn Time = 0.000447 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 57.43 s ClockTime = 58 s +Courant Number mean: 0.000650044 max: 0.0179773 +Time = 0.0007775 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 13273 + Current mass in system = 1.1984e-09 + Linear momentum = (2.96382e-11 -1.03094e-08 0) + |Linear momentum| = 1.03094e-08 + Linear kinetic energy = 4.6831e-08 + model1: + number of parcels added = 13285 + mass introduced = 1.22813e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.135, 523.009 + Mass transfer phase change = 2.97239e-11 + D10, D32, Dmax (mu) = 50.2762, 81.756, 149.767 + Liquid penetration 95% mass (m) = 0.00597708 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00442549, Final residual = 7.33998e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0123548, Final residual = 3.10218e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00204263, Final residual = 1.15439e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00245971, Final residual = 1.2613e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00273335, Final residual = 1.62857e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00273336, Final residual = 1.62983e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00193567, Final residual = 9.744e-08, No Iterations 1 +min/max(T) = 613.534, 930.917 +GAMG: Solving for p, Initial residual = 0.0376291, Final residual = 0.0001138, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.59868e-06, global = 2.56327e-06, cumulative = 0.000683711 +GAMG: Solving for p, Initial residual = 0.000109426, Final residual = 1.49639e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.5672e-06, global = 2.56716e-06, cumulative = 0.000686278 +smoothSolver: Solving for epsilon, Initial residual = 0.00101354, Final residual = 1.60019e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00255096, Final residual = 4.11867e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.096897 s +other Time = 0 s +rho Equations = 0.000174 s +U Equations = 0.001117 s +Y Equations = 0.00240645 s +E Equations = 0.000604 s +p Equations = 0.002163 s +calculate parcels = 30.2968 s +chemistry correctThermo = 0.002776 s +turbulence correct = 0.001022 s +combustion correct(in Y) = 0.0864375 s +percentage of chemistry = 89.2056 % +percentage of rho/U/Y/E = 4.4392 % +========Time details of each equation======= +rhoEqn Time = 0.000311 s +rhoEqn assamble = 0.000242 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001116 s +UEqn assamble = 0.000673 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000443 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001764 s +YEqn assamble = 0.000656 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000184 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000339 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 57.75 s ClockTime = 58 s +Courant Number mean: 0.000658921 max: 0.0179689 +Time = 0.00078 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 52 new parcels + +Cloud: sprayCloud + Current number of parcels = 13325 + Current mass in system = 1.20162e-09 + Linear momentum = (2.92413e-11 -1.03255e-08 0) + |Linear momentum| = 1.03255e-08 + Linear kinetic energy = 4.68481e-08 + model1: + number of parcels added = 13337 + mass introduced = 1.23156e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.141, 525.23 + Mass transfer phase change = 2.99476e-11 + D10, D32, Dmax (mu) = 50.3039, 81.8106, 149.931 + Liquid penetration 95% mass (m) = 0.00599447 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00439114, Final residual = 7.27872e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0123514, Final residual = 3.09666e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00202937, Final residual = 1.14435e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00245754, Final residual = 1.26334e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0027326, Final residual = 1.63244e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00273261, Final residual = 1.63373e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00193104, Final residual = 9.64949e-08, No Iterations 1 +min/max(T) = 613.582, 932.308 +GAMG: Solving for p, Initial residual = 0.0385809, Final residual = 0.000113003, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.61022e-06, global = 2.57468e-06, cumulative = 0.000688853 +GAMG: Solving for p, Initial residual = 0.000109661, Final residual = 8.24574e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.57781e-06, global = 2.57755e-06, cumulative = 0.00069143 +smoothSolver: Solving for epsilon, Initial residual = 0.0010112, Final residual = 1.5898e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00253664, Final residual = 4.09171e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.078101 s +other Time = 0 s +rho Equations = 0.000146 s +U Equations = 0.000931 s +Y Equations = 0.00200717 s +E Equations = 0.000491 s +p Equations = 0.001718 s +calculate parcels = 30.5163 s +chemistry correctThermo = 0.00205 s +turbulence correct = 0.000933 s +combustion correct(in Y) = 0.0696488 s +percentage of chemistry = 89.1779 % +percentage of rho/U/Y/E = 4.57763 % +========Time details of each equation======= +rhoEqn Time = 0.000266 s +rhoEqn assamble = 0.000211 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00093 s +UEqn assamble = 0.000568 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000362 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001457 s +YEqn assamble = 0.000554 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00014 s +YEqn correct boundary = 0 s +EEqn Time = 0.000373 s +EEqn assamble = 0.00028 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 58.05 s ClockTime = 58 s +Courant Number mean: 0.000667895 max: 0.0179639 +Time = 0.0007825 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 55 new parcels + +Cloud: sprayCloud + Current number of parcels = 13380 + Current mass in system = 1.20502e-09 + Linear momentum = (2.81204e-11 -1.03436e-08 0) + |Linear momentum| = 1.03436e-08 + Linear kinetic energy = 4.68752e-08 + model1: + number of parcels added = 13392 + mass introduced = 1.2352e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.151, 527.212 + Mass transfer phase change = 3.01721e-11 + D10, D32, Dmax (mu) = 50.3263, 81.8604, 149.927 + Liquid penetration 95% mass (m) = 0.00600998 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00445353, Final residual = 7.41059e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0123308, Final residual = 3.08892e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0020209, Final residual = 1.14232e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00245565, Final residual = 1.26375e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00273229, Final residual = 1.63668e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0027323, Final residual = 1.63796e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00192859, Final residual = 9.58241e-08, No Iterations 1 +min/max(T) = 613.634, 933.712 +GAMG: Solving for p, Initial residual = 0.0395397, Final residual = 0.000107825, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.61672e-06, global = 2.58577e-06, cumulative = 0.000694016 +GAMG: Solving for p, Initial residual = 0.000103968, Final residual = 9.21005e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.58834e-06, global = 2.58807e-06, cumulative = 0.000696604 +smoothSolver: Solving for epsilon, Initial residual = 0.00100931, Final residual = 1.5805e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00252343, Final residual = 4.06621e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.089093 s +other Time = 0 s +rho Equations = 0.000142 s +U Equations = 0.001159 s +Y Equations = 0.00242523 s +E Equations = 0.000601 s +p Equations = 0.002039 s +calculate parcels = 30.7525 s +chemistry correctThermo = 0.002778 s +turbulence correct = 0.000959 s +combustion correct(in Y) = 0.0788188 s +percentage of chemistry = 88.468 % +percentage of rho/U/Y/E = 4.85699 % +========Time details of each equation======= +rhoEqn Time = 0.000299 s +rhoEqn assamble = 0.000227 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001158 s +UEqn assamble = 0.00071 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000448 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001775 s +YEqn assamble = 0.000655 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00017 s +YEqn correct boundary = 0 s +EEqn Time = 0.000445 s +EEqn assamble = 0.000331 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 58.37 s ClockTime = 59 s +Courant Number mean: 0.000676922 max: 0.0179561 +Time = 0.000785 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 43 new parcels + +Cloud: sprayCloud + Current number of parcels = 13423 + Current mass in system = 1.20764e-09 + Linear momentum = (2.85169e-11 -1.03539e-08 0) + |Linear momentum| = 1.03539e-08 + Linear kinetic energy = 4.68637e-08 + model1: + number of parcels added = 13435 + mass introduced = 1.23804e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.143, 527.72 + Mass transfer phase change = 3.03975e-11 + D10, D32, Dmax (mu) = 50.325, 81.8851, 149.899 + Liquid penetration 95% mass (m) = 0.00602665 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00451722, Final residual = 7.58373e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0123197, Final residual = 3.09468e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00202052, Final residual = 1.14852e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00245381, Final residual = 1.26823e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00273245, Final residual = 1.63974e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00273247, Final residual = 1.64102e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00192454, Final residual = 9.51695e-08, No Iterations 1 +min/max(T) = 613.7, 935.129 +GAMG: Solving for p, Initial residual = 0.0407173, Final residual = 0.00013135, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.62885e-06, global = 2.59587e-06, cumulative = 0.0006992 +GAMG: Solving for p, Initial residual = 0.00012888, Final residual = 1.42039e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.59843e-06, global = 2.59839e-06, cumulative = 0.000701798 +smoothSolver: Solving for epsilon, Initial residual = 0.00100703, Final residual = 1.5724e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0025112, Final residual = 4.04135e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.096481 s +other Time = 1e-06 s +rho Equations = 0.000171 s +U Equations = 0.001103 s +Y Equations = 0.0023239 s +E Equations = 0.000655 s +p Equations = 0.002233 s +calculate parcels = 30.9778 s +chemistry correctThermo = 0.002775 s +turbulence correct = 0.001038 s +combustion correct(in Y) = 0.0859811 s +percentage of chemistry = 89.1171 % +percentage of rho/U/Y/E = 4.40802 % +========Time details of each equation======= +rhoEqn Time = 0.000316 s +rhoEqn assamble = 0.00025 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001102 s +UEqn assamble = 0.000667 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000435 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00168 s +YEqn assamble = 0.000635 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000167 s +YEqn correct boundary = 0 s +EEqn Time = 0.0005 s +EEqn assamble = 0.00037 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00013 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 58.7 s ClockTime = 59 s +Courant Number mean: 0.000686 max: 0.0179295 +Time = 0.0007875 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 60 new parcels + +Cloud: sprayCloud + Current number of parcels = 13483 + Current mass in system = 1.21137e-09 + Linear momentum = (2.73056e-11 -1.03751e-08 0) + |Linear momentum| = 1.03751e-08 + Linear kinetic energy = 4.69066e-08 + model1: + number of parcels added = 13495 + mass introduced = 1.24199e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.154, 528.038 + Mass transfer phase change = 3.06238e-11 + D10, D32, Dmax (mu) = 50.3496, 81.9342, 149.853 + Liquid penetration 95% mass (m) = 0.00604386 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00457612, Final residual = 7.59149e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0122957, Final residual = 3.09466e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00201826, Final residual = 1.1444e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00245172, Final residual = 1.27028e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0027325, Final residual = 1.64357e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00273252, Final residual = 1.64487e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00192346, Final residual = 9.53221e-08, No Iterations 1 +min/max(T) = 613.792, 936.559 +GAMG: Solving for p, Initial residual = 0.0416968, Final residual = 0.000122827, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.6393e-06, global = 2.60545e-06, cumulative = 0.000704404 +GAMG: Solving for p, Initial residual = 0.000119728, Final residual = 9.13524e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.60803e-06, global = 2.60778e-06, cumulative = 0.000707011 +smoothSolver: Solving for epsilon, Initial residual = 0.00100485, Final residual = 1.56564e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00249896, Final residual = 4.01772e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.099139 s +other Time = 0 s +rho Equations = 0.000182 s +U Equations = 0.001203 s +Y Equations = 0.00236896 s +E Equations = 0.000654 s +p Equations = 0.002025 s +calculate parcels = 31.1899 s +chemistry correctThermo = 0.002776 s +turbulence correct = 0.00102 s +combustion correct(in Y) = 0.088689 s +percentage of chemistry = 89.4593 % +percentage of rho/U/Y/E = 4.44624 % +========Time details of each equation======= +rhoEqn Time = 0.000321 s +rhoEqn assamble = 0.000244 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001202 s +UEqn assamble = 0.000717 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000485 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001689 s +YEqn assamble = 0.000624 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000164 s +YEqn correct boundary = 0 s +EEqn Time = 0.000501 s +EEqn assamble = 0.000384 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 59.01 s ClockTime = 59 s +Courant Number mean: 0.000695129 max: 0.0179078 +Time = 0.00079 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 52 new parcels + +Cloud: sprayCloud + Current number of parcels = 13535 + Current mass in system = 1.21458e-09 + Linear momentum = (2.76265e-11 -1.03912e-08 0) + |Linear momentum| = 1.03912e-08 + Linear kinetic energy = 4.69245e-08 + model1: + number of parcels added = 13547 + mass introduced = 1.24543e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.141, 528.268 + Mass transfer phase change = 3.08508e-11 + D10, D32, Dmax (mu) = 50.3648, 81.9805, 149.795 + Liquid penetration 95% mass (m) = 0.00606075 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00444899, Final residual = 7.42445e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0122846, Final residual = 3.09139e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00201712, Final residual = 1.15448e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00244981, Final residual = 1.27081e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00273281, Final residual = 1.64763e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00273283, Final residual = 1.64893e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00192262, Final residual = 9.52336e-08, No Iterations 1 +min/max(T) = 613.905, 938.003 +GAMG: Solving for p, Initial residual = 0.0425525, Final residual = 0.000109592, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.64628e-06, global = 2.61397e-06, cumulative = 0.000709625 +GAMG: Solving for p, Initial residual = 0.000106598, Final residual = 8.71111e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.61677e-06, global = 2.61651e-06, cumulative = 0.000712242 +smoothSolver: Solving for epsilon, Initial residual = 0.00100286, Final residual = 1.55932e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00248667, Final residual = 3.99403e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.082525 s +other Time = 0 s +rho Equations = 0.000174 s +U Equations = 0.001162 s +Y Equations = 0.00229869 s +E Equations = 0.00051 s +p Equations = 0.001713 s +calculate parcels = 31.4127 s +chemistry correctThermo = 0.002033 s +turbulence correct = 0.000837 s +combustion correct(in Y) = 0.0735773 s +percentage of chemistry = 89.1576 % +percentage of rho/U/Y/E = 5.02235 % +========Time details of each equation======= +rhoEqn Time = 0.000296 s +rhoEqn assamble = 0.000236 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001162 s +UEqn assamble = 0.000708 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000454 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001618 s +YEqn assamble = 0.000629 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.9e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000382 s +EEqn assamble = 0.000285 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.7e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 59.31 s ClockTime = 60 s +Courant Number mean: 0.000704287 max: 0.0178874 +Time = 0.0007925 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 59 new parcels + +Cloud: sprayCloud + Current number of parcels = 13594 + Current mass in system = 1.21825e-09 + Linear momentum = (2.77551e-11 -1.04119e-08 0) + |Linear momentum| = 1.04119e-08 + Linear kinetic energy = 4.69651e-08 + model1: + number of parcels added = 13606 + mass introduced = 1.24933e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.142, 528.42 + Mass transfer phase change = 3.10785e-11 + D10, D32, Dmax (mu) = 50.3765, 82.0304, 149.801 + Liquid penetration 95% mass (m) = 0.00607672 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00437664, Final residual = 7.35518e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0122701, Final residual = 3.09623e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00201055, Final residual = 1.15389e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00244775, Final residual = 1.27302e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00273286, Final residual = 1.65167e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00273288, Final residual = 1.65298e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00192286, Final residual = 9.50139e-08, No Iterations 1 +min/max(T) = 614.042, 939.461 +GAMG: Solving for p, Initial residual = 0.0434468, Final residual = 9.4207e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.65015e-06, global = 2.62383e-06, cumulative = 0.000714866 +GAMG: Solving for p, Initial residual = 9.14294e-05, Final residual = 7.52765e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.62508e-06, global = 2.62485e-06, cumulative = 0.000717491 +smoothSolver: Solving for epsilon, Initial residual = 0.00100086, Final residual = 1.55274e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00247458, Final residual = 3.97097e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.070978 s +other Time = 0 s +rho Equations = 0.000157 s +U Equations = 0.001054 s +Y Equations = 0.00237199 s +E Equations = 0.000519 s +p Equations = 0.002166 s +calculate parcels = 31.5803 s +chemistry correctThermo = 0.002007 s +turbulence correct = 0.001001 s +combustion correct(in Y) = 0.061513 s +percentage of chemistry = 86.6649 % +percentage of rho/U/Y/E = 5.77923 % +========Time details of each equation======= +rhoEqn Time = 0.000323 s +rhoEqn assamble = 0.000265 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001054 s +UEqn assamble = 0.000686 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000368 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001814 s +YEqn assamble = 0.000593 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000235 s +YEqn correct boundary = 0 s +EEqn Time = 0.000389 s +EEqn assamble = 0.000289 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.0001 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 59.55 s ClockTime = 60 s +Courant Number mean: 0.000713498 max: 0.0178685 +Time = 0.000795 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 43 new parcels + +Cloud: sprayCloud + Current number of parcels = 13637 + Current mass in system = 1.22087e-09 + Linear momentum = (2.83008e-11 -1.04224e-08 0) + |Linear momentum| = 1.04224e-08 + Linear kinetic energy = 4.69557e-08 + model1: + number of parcels added = 13649 + mass introduced = 1.25218e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.138, 528.496 + Mass transfer phase change = 3.13071e-11 + D10, D32, Dmax (mu) = 50.3929, 82.0684, 149.807 + Liquid penetration 95% mass (m) = 0.0060923 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00443627, Final residual = 7.52344e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0122322, Final residual = 3.09328e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00200487, Final residual = 1.15454e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00244637, Final residual = 1.27339e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00273373, Final residual = 1.6555e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00273374, Final residual = 1.65681e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00192114, Final residual = 9.46163e-08, No Iterations 1 +min/max(T) = 614.189, 940.934 +GAMG: Solving for p, Initial residual = 0.0444662, Final residual = 9.61871e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.6591e-06, global = 2.63275e-06, cumulative = 0.000720123 +GAMG: Solving for p, Initial residual = 9.35823e-05, Final residual = 7.55287e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.63403e-06, global = 2.6338e-06, cumulative = 0.000722757 +smoothSolver: Solving for epsilon, Initial residual = 0.000998265, Final residual = 1.54582e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00246429, Final residual = 3.95215e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.093062 s +other Time = 0 s +rho Equations = 0.000172 s +U Equations = 0.001123 s +Y Equations = 0.00242682 s +E Equations = 0.000541 s +p Equations = 0.002525 s +calculate parcels = 31.7802 s +chemistry correctThermo = 0.001974 s +turbulence correct = 0.001609 s +combustion correct(in Y) = 0.0824912 s +percentage of chemistry = 88.6411 % +percentage of rho/U/Y/E = 4.58062 % +========Time details of each equation======= +rhoEqn Time = 0.000362 s +rhoEqn assamble = 0.00028 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001122 s +UEqn assamble = 0.000672 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00045 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001773 s +YEqn assamble = 0.00066 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000177 s +YEqn correct boundary = 0 s +EEqn Time = 0.000401 s +EEqn assamble = 0.000303 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 59.85 s ClockTime = 60 s +Courant Number mean: 0.000722759 max: 0.0178477 +Time = 0.0007975 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 40 new parcels + +Cloud: sprayCloud + Current number of parcels = 13677 + Current mass in system = 1.22329e-09 + Linear momentum = (2.85574e-11 -1.04309e-08 0) + |Linear momentum| = 1.0431e-08 + Linear kinetic energy = 4.69371e-08 + model1: + number of parcels added = 13689 + mass introduced = 1.25483e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.139, 528.485 + Mass transfer phase change = 3.15364e-11 + D10, D32, Dmax (mu) = 50.37, 82.083, 149.813 + Liquid penetration 95% mass (m) = 0.00610809 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00455008, Final residual = 7.70695e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0121753, Final residual = 3.08023e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00200053, Final residual = 1.15009e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00244525, Final residual = 1.27113e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00273466, Final residual = 1.65848e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00273467, Final residual = 1.6598e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00192102, Final residual = 9.43903e-08, No Iterations 1 +min/max(T) = 614.353, 942.42 +GAMG: Solving for p, Initial residual = 0.0453326, Final residual = 7.82697e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.66446e-06, global = 2.64282e-06, cumulative = 0.0007254 +GAMG: Solving for p, Initial residual = 7.60664e-05, Final residual = 5.55754e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.64357e-06, global = 2.64341e-06, cumulative = 0.000728043 +smoothSolver: Solving for epsilon, Initial residual = 0.000995548, Final residual = 1.53857e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00245501, Final residual = 3.93609e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103128 s +other Time = 0 s +rho Equations = 0.000175 s +U Equations = 0.00111 s +Y Equations = 0.00209859 s +E Equations = 0.000493 s +p Equations = 0.001622 s +calculate parcels = 32.0272 s +chemistry correctThermo = 0.001966 s +turbulence correct = 0.000835 s +combustion correct(in Y) = 0.0946434 s +percentage of chemistry = 91.7728 % +percentage of rho/U/Y/E = 3.75901 % +========Time details of each equation======= +rhoEqn Time = 0.000298 s +rhoEqn assamble = 0.000235 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001109 s +UEqn assamble = 0.000666 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000443 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001447 s +YEqn assamble = 0.000548 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.1e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000376 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 60.2 s ClockTime = 61 s +Courant Number mean: 0.000732096 max: 0.0178291 +Time = 0.0008 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 41 new parcels + +Cloud: sprayCloud + Current number of parcels = 13718 + Current mass in system = 1.22577e-09 + Linear momentum = (2.78744e-11 -1.04401e-08 0) + |Linear momentum| = 1.04401e-08 + Linear kinetic energy = 4.69219e-08 + model1: + number of parcels added = 13730 + mass introduced = 1.25754e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.144, 528.378 + Mass transfer phase change = 3.17666e-11 + D10, D32, Dmax (mu) = 50.2593, 82.0918, 149.818 + Liquid penetration 95% mass (m) = 0.00612305 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00459572, Final residual = 7.74783e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0121105, Final residual = 3.06017e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00199378, Final residual = 1.15615e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00244399, Final residual = 1.27347e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00273536, Final residual = 1.66138e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00273537, Final residual = 1.66269e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00191905, Final residual = 9.43173e-08, No Iterations 1 +min/max(T) = 614.526, 943.92 +GAMG: Solving for p, Initial residual = 0.0461965, Final residual = 7.59347e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.67172e-06, global = 2.65316e-06, cumulative = 0.000730697 +GAMG: Solving for p, Initial residual = 7.38229e-05, Final residual = 7.03452e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.65339e-06, global = 2.65321e-06, cumulative = 0.00073335 +smoothSolver: Solving for epsilon, Initial residual = 0.000992921, Final residual = 1.53076e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00244502, Final residual = 3.92051e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.086313 s +other Time = 0 s +rho Equations = 0.000241 s +U Equations = 0.001263 s +Y Equations = 0.00258907 s +E Equations = 0.000636 s +p Equations = 0.002033 s +calculate parcels = 32.2772 s +chemistry correctThermo = 0.002802 s +turbulence correct = 0.001009 s +combustion correct(in Y) = 0.0755539 s +percentage of chemistry = 87.5348 % +percentage of rho/U/Y/E = 5.47898 % +========Time details of each equation======= +rhoEqn Time = 0.000385 s +rhoEqn assamble = 0.00031 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001262 s +UEqn assamble = 0.00081 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000452 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00192 s +YEqn assamble = 0.00077 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000185 s +YEqn correct boundary = 0 s +EEqn Time = 0.000479 s +EEqn assamble = 0.000357 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000122 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 60.76 s ClockTime = 61 s +Courant Number mean: 0.000741497 max: 0.0178091 +Time = 0.0008025 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 13766 + Current mass in system = 1.2287e-09 + Linear momentum = (2.79493e-11 -1.04537e-08 0) + |Linear momentum| = 1.04538e-08 + Linear kinetic energy = 4.69296e-08 + model1: + number of parcels added = 13778 + mass introduced = 1.2607e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.15, 529.6 + Mass transfer phase change = 3.19976e-11 + D10, D32, Dmax (mu) = 49.6098, 82.1067, 149.824 + Liquid penetration 95% mass (m) = 0.00613929 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00461607, Final residual = 7.84817e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0120351, Final residual = 3.03577e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00199173, Final residual = 1.15984e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00244295, Final residual = 1.27745e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00273649, Final residual = 1.66384e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0027365, Final residual = 1.66516e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00191903, Final residual = 9.40607e-08, No Iterations 1 +min/max(T) = 614.72, 945.435 +GAMG: Solving for p, Initial residual = 0.0471327, Final residual = 7.7435e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.68255e-06, global = 2.66242e-06, cumulative = 0.000736012 +GAMG: Solving for p, Initial residual = 7.48965e-05, Final residual = 6.6378e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.66311e-06, global = 2.66292e-06, cumulative = 0.000738675 +smoothSolver: Solving for epsilon, Initial residual = 0.000990482, Final residual = 1.52238e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00243497, Final residual = 3.9042e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.086053 s +other Time = 1e-06 s +rho Equations = 0.00016 s +U Equations = 0.001119 s +Y Equations = 0.00237444 s +E Equations = 0.000599 s +p Equations = 0.001946 s +calculate parcels = 32.4585 s +chemistry correctThermo = 0.002746 s +turbulence correct = 0.00091 s +combustion correct(in Y) = 0.0760076 s +percentage of chemistry = 88.3264 % +percentage of rho/U/Y/E = 4.94165 % +========Time details of each equation======= +rhoEqn Time = 0.000311 s +rhoEqn assamble = 0.000245 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001118 s +UEqn assamble = 0.000685 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000433 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001735 s +YEqn assamble = 0.00065 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000174 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 61.03 s ClockTime = 61 s +Courant Number mean: 0.000750969 max: 0.0178027 +Time = 0.000805 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 59 new parcels + +Cloud: sprayCloud + Current number of parcels = 13825 + Current mass in system = 1.23236e-09 + Linear momentum = (2.79895e-11 -1.04746e-08 0) + |Linear momentum| = 1.04746e-08 + Linear kinetic energy = 4.69734e-08 + model1: + number of parcels added = 13837 + mass introduced = 1.26458e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.149, 531.301 + Mass transfer phase change = 3.22295e-11 + D10, D32, Dmax (mu) = 49.4196, 82.1109, 149.83 + Liquid penetration 95% mass (m) = 0.00615503 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00462734, Final residual = 7.89248e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0119507, Final residual = 3.01727e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0020003, Final residual = 1.15292e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00244185, Final residual = 1.27653e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00273761, Final residual = 1.66658e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00273762, Final residual = 1.6679e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00192189, Final residual = 9.41372e-08, No Iterations 1 +min/max(T) = 614.919, 946.963 +GAMG: Solving for p, Initial residual = 0.048138, Final residual = 9.98461e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.69927e-06, global = 2.67141e-06, cumulative = 0.000741346 +GAMG: Solving for p, Initial residual = 9.68383e-05, Final residual = 8.42724e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.67284e-06, global = 2.6726e-06, cumulative = 0.000744019 +smoothSolver: Solving for epsilon, Initial residual = 0.00098801, Final residual = 1.51453e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00242532, Final residual = 3.88796e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.096794 s +other Time = 1e-06 s +rho Equations = 0.000182 s +U Equations = 0.001148 s +Y Equations = 0.00242525 s +E Equations = 0.000613 s +p Equations = 0.002048 s +calculate parcels = 32.6613 s +chemistry correctThermo = 0.002786 s +turbulence correct = 0.001022 s +combustion correct(in Y) = 0.0863667 s +percentage of chemistry = 89.2274 % +percentage of rho/U/Y/E = 4.51294 % +========Time details of each equation======= +rhoEqn Time = 0.000341 s +rhoEqn assamble = 0.00026 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001147 s +UEqn assamble = 0.000696 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000451 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001766 s +YEqn assamble = 0.000659 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000171 s +YEqn correct boundary = 0 s +EEqn Time = 0.000461 s +EEqn assamble = 0.000346 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 61.33 s ClockTime = 62 s +Courant Number mean: 0.000760479 max: 0.0177874 +Time = 0.0008075 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 55 new parcels + +Cloud: sprayCloud + Current number of parcels = 13880 + Current mass in system = 1.23576e-09 + Linear momentum = (2.74872e-11 -1.04931e-08 0) + |Linear momentum| = 1.04931e-08 + Linear kinetic energy = 4.70056e-08 + model1: + number of parcels added = 13892 + mass introduced = 1.26823e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.139, 532.735 + Mass transfer phase change = 3.24623e-11 + D10, D32, Dmax (mu) = 49.3999, 82.1342, 149.836 + Liquid penetration 95% mass (m) = 0.00617008 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00468984, Final residual = 8.03094e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0118661, Final residual = 3.0037e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0019917, Final residual = 1.15372e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00244119, Final residual = 1.28097e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00273897, Final residual = 1.66862e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00273898, Final residual = 1.66994e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00192159, Final residual = 9.44791e-08, No Iterations 1 +min/max(T) = 615.137, 948.506 +GAMG: Solving for p, Initial residual = 0.0487526, Final residual = 8.7366e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.70656e-06, global = 2.68209e-06, cumulative = 0.000746701 +GAMG: Solving for p, Initial residual = 8.47208e-05, Final residual = 7.19692e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.68337e-06, global = 2.68318e-06, cumulative = 0.000749384 +smoothSolver: Solving for epsilon, Initial residual = 0.000984885, Final residual = 1.50618e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00241518, Final residual = 3.87091e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.084382 s +other Time = 0 s +rho Equations = 0.000142 s +U Equations = 0.000943 s +Y Equations = 0.00206271 s +E Equations = 0.000508 s +p Equations = 0.001674 s +calculate parcels = 32.8818 s +chemistry correctThermo = 0.001968 s +turbulence correct = 0.000828 s +combustion correct(in Y) = 0.0760873 s +percentage of chemistry = 90.17 % +percentage of rho/U/Y/E = 4.33233 % +========Time details of each equation======= +rhoEqn Time = 0.000262 s +rhoEqn assamble = 0.000207 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000943 s +UEqn assamble = 0.000572 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000371 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001508 s +YEqn assamble = 0.000548 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000165 s +YEqn correct boundary = 0 s +EEqn Time = 0.000379 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 61.63 s ClockTime = 62 s +Courant Number mean: 0.000770058 max: 0.0177576 +Time = 0.00081 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 43 new parcels + +Cloud: sprayCloud + Current number of parcels = 13923 + Current mass in system = 1.23839e-09 + Linear momentum = (2.76529e-11 -1.05039e-08 0) + |Linear momentum| = 1.05039e-08 + Linear kinetic energy = 4.7e-08 + model1: + number of parcels added = 13935 + mass introduced = 1.27108e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.143, 533.934 + Mass transfer phase change = 3.26959e-11 + D10, D32, Dmax (mu) = 49.408, 82.1751, 149.842 + Liquid penetration 95% mass (m) = 0.00618437 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00467958, Final residual = 8.13011e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0117607, Final residual = 2.97101e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00198179, Final residual = 1.14387e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0024403, Final residual = 1.2792e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00274042, Final residual = 1.67263e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00274043, Final residual = 1.67395e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00191662, Final residual = 9.35358e-08, No Iterations 1 +min/max(T) = 615.376, 950.065 +GAMG: Solving for p, Initial residual = 0.0496454, Final residual = 0.000120113, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.72513e-06, global = 2.69068e-06, cumulative = 0.000752075 +GAMG: Solving for p, Initial residual = 0.00011792, Final residual = 2.28035e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.69244e-06, global = 2.69237e-06, cumulative = 0.000754767 +smoothSolver: Solving for epsilon, Initial residual = 0.000981402, Final residual = 1.49708e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00240448, Final residual = 3.85262e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.069577 s +other Time = 0 s +rho Equations = 0.000163 s +U Equations = 0.001013 s +Y Equations = 0.00217271 s +E Equations = 0.000503 s +p Equations = 0.002099 s +calculate parcels = 33.07 s +chemistry correctThermo = 0.002116 s +turbulence correct = 0.000892 s +combustion correct(in Y) = 0.0604243 s +percentage of chemistry = 86.8452 % +percentage of rho/U/Y/E = 5.5359 % +========Time details of each equation======= +rhoEqn Time = 0.00029 s +rhoEqn assamble = 0.000231 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001013 s +UEqn assamble = 0.000638 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000375 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001714 s +YEqn assamble = 0.000627 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000143 s +YEqn correct boundary = 0 s +EEqn Time = 0.000379 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 61.89 s ClockTime = 62 s +Courant Number mean: 0.000779662 max: 0.0177484 +Time = 0.0008125 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 13967 + Current mass in system = 1.24107e-09 + Linear momentum = (2.75335e-11 -1.05153e-08 0) + |Linear momentum| = 1.05153e-08 + Linear kinetic energy = 4.6998e-08 + model1: + number of parcels added = 13979 + mass introduced = 1.274e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.165, 534.922 + Mass transfer phase change = 3.29303e-11 + D10, D32, Dmax (mu) = 49.3426, 82.1768, 149.848 + Liquid penetration 95% mass (m) = 0.00620107 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00482713, Final residual = 8.33341e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0116105, Final residual = 2.92633e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00197524, Final residual = 1.13761e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00243997, Final residual = 1.27569e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00274212, Final residual = 1.67645e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00274213, Final residual = 1.67777e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00191558, Final residual = 9.26446e-08, No Iterations 1 +min/max(T) = 615.634, 951.639 +GAMG: Solving for p, Initial residual = 0.0505445, Final residual = 0.000110532, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.73242e-06, global = 2.70116e-06, cumulative = 0.000757469 +GAMG: Solving for p, Initial residual = 0.00010651, Final residual = 9.90552e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.70246e-06, global = 2.70216e-06, cumulative = 0.000760171 +smoothSolver: Solving for epsilon, Initial residual = 0.000978256, Final residual = 1.48853e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00239433, Final residual = 3.83547e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097269 s +other Time = 1e-06 s +rho Equations = 0.000174 s +U Equations = 0.001111 s +Y Equations = 0.0020522 s +E Equations = 0.000624 s +p Equations = 0.001721 s +calculate parcels = 33.249 s +chemistry correctThermo = 0.002035 s +turbulence correct = 0.000853 s +combustion correct(in Y) = 0.0884878 s +percentage of chemistry = 90.9723 % +percentage of rho/U/Y/E = 4.07242 % +========Time details of each equation======= +rhoEqn Time = 0.000296 s +rhoEqn assamble = 0.000231 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00111 s +UEqn assamble = 0.00068 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00043 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001425 s +YEqn assamble = 0.000532 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000508 s +EEqn assamble = 0.0004 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000108 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 62.17 s ClockTime = 63 s +Courant Number mean: 0.000789252 max: 0.0177331 +Time = 0.000815 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 54 new parcels + +Cloud: sprayCloud + Current number of parcels = 14021 + Current mass in system = 1.24441e-09 + Linear momentum = (2.7167e-11 -1.05333e-08 0) + |Linear momentum| = 1.05333e-08 + Linear kinetic energy = 4.70291e-08 + model1: + number of parcels added = 14033 + mass introduced = 1.27757e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.142, 535.727 + Mass transfer phase change = 3.31656e-11 + D10, D32, Dmax (mu) = 49.3313, 82.2032, 149.853 + Liquid penetration 95% mass (m) = 0.0062175 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00474236, Final residual = 8.14363e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0115021, Final residual = 2.90537e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00196736, Final residual = 1.14841e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00243952, Final residual = 1.27803e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00274361, Final residual = 1.68051e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00274362, Final residual = 1.68187e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00191686, Final residual = 9.25845e-08, No Iterations 1 +min/max(T) = 615.908, 953.229 +GAMG: Solving for p, Initial residual = 0.0512106, Final residual = 0.000114075, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.74199e-06, global = 2.71025e-06, cumulative = 0.000762881 +GAMG: Solving for p, Initial residual = 0.000110679, Final residual = 8.98579e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.71169e-06, global = 2.71143e-06, cumulative = 0.000765592 +smoothSolver: Solving for epsilon, Initial residual = 0.000974974, Final residual = 1.47967e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00238445, Final residual = 3.81921e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.082008 s +other Time = 0 s +rho Equations = 0.000195 s +U Equations = 0.001145 s +Y Equations = 0.00237297 s +E Equations = 0.000496 s +p Equations = 0.00176 s +calculate parcels = 33.4592 s +chemistry correctThermo = 0.002067 s +turbulence correct = 0.001052 s +combustion correct(in Y) = 0.072722 s +percentage of chemistry = 88.6768 % +percentage of rho/U/Y/E = 5.13239 % +========Time details of each equation======= +rhoEqn Time = 0.000318 s +rhoEqn assamble = 0.000251 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001144 s +UEqn assamble = 0.000683 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000461 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001656 s +YEqn assamble = 0.00061 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000145 s +YEqn correct boundary = 0 s +EEqn Time = 0.000375 s +EEqn assamble = 0.000279 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 62.46 s ClockTime = 63 s +Courant Number mean: 0.000798788 max: 0.0177028 +Time = 0.0008175 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 14070 + Current mass in system = 1.24742e-09 + Linear momentum = (2.79202e-11 -1.05482e-08 0) + |Linear momentum| = 1.05482e-08 + Linear kinetic energy = 4.7045e-08 + model1: + number of parcels added = 14082 + mass introduced = 1.28082e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.149, 536.376 + Mass transfer phase change = 3.34017e-11 + D10, D32, Dmax (mu) = 49.3205, 82.2366, 149.859 + Liquid penetration 95% mass (m) = 0.00623259 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00469219, Final residual = 8.03895e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0113895, Final residual = 2.88844e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00195673, Final residual = 1.155e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00243971, Final residual = 1.28e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00274589, Final residual = 1.68481e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0027459, Final residual = 1.68619e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00191725, Final residual = 9.24068e-08, No Iterations 1 +min/max(T) = 616.2, 954.834 +GAMG: Solving for p, Initial residual = 0.0517781, Final residual = 0.00010943, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.7489e-06, global = 2.72001e-06, cumulative = 0.000768312 +GAMG: Solving for p, Initial residual = 0.000106032, Final residual = 7.18371e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.72116e-06, global = 2.72096e-06, cumulative = 0.000771033 +smoothSolver: Solving for epsilon, Initial residual = 0.000971292, Final residual = 1.4706e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00237446, Final residual = 3.80271e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.081085 s +other Time = 0 s +rho Equations = 0.000173 s +U Equations = 0.001166 s +Y Equations = 0.00203017 s +E Equations = 0.000483 s +p Equations = 0.001562 s +calculate parcels = 33.6941 s +chemistry correctThermo = 0.001974 s +turbulence correct = 0.000831 s +combustion correct(in Y) = 0.0726788 s +percentage of chemistry = 89.6329 % +percentage of rho/U/Y/E = 4.75077 % +========Time details of each equation======= +rhoEqn Time = 0.000285 s +rhoEqn assamble = 0.000223 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001166 s +UEqn assamble = 0.000704 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000462 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001385 s +YEqn assamble = 0.000528 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.7e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000366 s +EEqn assamble = 0.000273 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 62.77 s ClockTime = 63 s +Courant Number mean: 0.000808254 max: 0.0176682 +Time = 0.00082 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 14118 + Current mass in system = 1.25037e-09 + Linear momentum = (2.83435e-11 -1.05625e-08 0) + |Linear momentum| = 1.05625e-08 + Linear kinetic energy = 4.70584e-08 + model1: + number of parcels added = 14130 + mass introduced = 1.28401e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.145, 536.892 + Mass transfer phase change = 3.36385e-11 + D10, D32, Dmax (mu) = 49.1317, 82.2519, 149.865 + Liquid penetration 95% mass (m) = 0.00624997 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00474011, Final residual = 8.06189e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0112685, Final residual = 2.86751e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00194525, Final residual = 1.15603e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0024395, Final residual = 1.28454e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0027477, Final residual = 1.68918e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00274771, Final residual = 1.69057e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00191831, Final residual = 9.2051e-08, No Iterations 1 +min/max(T) = 616.496, 956.454 +GAMG: Solving for p, Initial residual = 0.0524471, Final residual = 0.000103415, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.75847e-06, global = 2.72928e-06, cumulative = 0.000773763 +GAMG: Solving for p, Initial residual = 0.000100763, Final residual = 7.53593e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.73058e-06, global = 2.73034e-06, cumulative = 0.000776493 +smoothSolver: Solving for epsilon, Initial residual = 0.000968077, Final residual = 1.46201e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00236477, Final residual = 3.78611e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094055 s +other Time = 1e-06 s +rho Equations = 0.000185 s +U Equations = 0.001306 s +Y Equations = 0.00246119 s +E Equations = 0.000605 s +p Equations = 0.002113 s +calculate parcels = 33.9228 s +chemistry correctThermo = 0.002774 s +turbulence correct = 0.001017 s +combustion correct(in Y) = 0.0833848 s +percentage of chemistry = 88.6554 % +percentage of rho/U/Y/E = 4.84524 % +========Time details of each equation======= +rhoEqn Time = 0.000353 s +rhoEqn assamble = 0.000277 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001305 s +UEqn assamble = 0.000804 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000501 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001741 s +YEqn assamble = 0.000658 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000154 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 63.1 s ClockTime = 64 s +Courant Number mean: 0.000817639 max: 0.0176469 +Time = 0.0008225 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 14167 + Current mass in system = 1.25339e-09 + Linear momentum = (2.80774e-11 -1.05775e-08 0) + |Linear momentum| = 1.05775e-08 + Linear kinetic energy = 4.70757e-08 + model1: + number of parcels added = 14179 + mass introduced = 1.28726e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.137, 536.323 + Mass transfer phase change = 3.38762e-11 + D10, D32, Dmax (mu) = 49.1125, 82.2862, 149.871 + Liquid penetration 95% mass (m) = 0.00626437 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00480112, Final residual = 8.09177e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0111593, Final residual = 2.85345e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00196188, Final residual = 1.20796e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00243968, Final residual = 1.30192e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00275028, Final residual = 1.69258e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00275028, Final residual = 1.69397e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00191753, Final residual = 9.24498e-08, No Iterations 1 +min/max(T) = 616.794, 958.09 +GAMG: Solving for p, Initial residual = 0.0532527, Final residual = 0.000117506, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.76985e-06, global = 2.7377e-06, cumulative = 0.000779231 +GAMG: Solving for p, Initial residual = 0.000115427, Final residual = 7.70998e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.73955e-06, global = 2.73932e-06, cumulative = 0.00078197 +smoothSolver: Solving for epsilon, Initial residual = 0.00096494, Final residual = 1.45349e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00235538, Final residual = 3.771e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.098439 s +other Time = 0 s +rho Equations = 0.000189 s +U Equations = 0.001172 s +Y Equations = 0.00260761 s +E Equations = 0.000537 s +p Equations = 0.002003 s +calculate parcels = 34.169 s +chemistry correctThermo = 0.002255 s +turbulence correct = 0.000939 s +combustion correct(in Y) = 0.0885214 s +percentage of chemistry = 89.9251 % +percentage of rho/U/Y/E = 4.57706 % +========Time details of each equation======= +rhoEqn Time = 0.000336 s +rhoEqn assamble = 0.000263 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001172 s +UEqn assamble = 0.000721 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000451 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001954 s +YEqn assamble = 0.000771 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000269 s +YEqn correct boundary = 0 s +EEqn Time = 0.000406 s +EEqn assamble = 0.000298 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000108 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 63.44 s ClockTime = 64 s +Courant Number mean: 0.000826945 max: 0.01764 +Time = 0.000825 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 14213 + Current mass in system = 1.25621e-09 + Linear momentum = (2.8628e-11 -1.05906e-08 0) + |Linear momentum| = 1.05907e-08 + Linear kinetic energy = 4.70842e-08 + model1: + number of parcels added = 14225 + mass introduced = 1.29032e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.151, 535.589 + Mass transfer phase change = 3.41146e-11 + D10, D32, Dmax (mu) = 49.0992, 82.3166, 149.877 + Liquid penetration 95% mass (m) = 0.00627953 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0048364, Final residual = 7.99613e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0110444, Final residual = 2.83448e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0019511, Final residual = 1.21412e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00243987, Final residual = 1.3038e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00275287, Final residual = 1.69693e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00275288, Final residual = 1.69833e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00191697, Final residual = 9.24168e-08, No Iterations 1 +min/max(T) = 617.099, 959.742 +GAMG: Solving for p, Initial residual = 0.0538332, Final residual = 0.000124663, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.78296e-06, global = 2.74632e-06, cumulative = 0.000784716 +GAMG: Solving for p, Initial residual = 0.00012209, Final residual = 7.60608e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.74784e-06, global = 2.7476e-06, cumulative = 0.000787464 +smoothSolver: Solving for epsilon, Initial residual = 0.000961731, Final residual = 1.4452e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.002345, Final residual = 3.75271e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09241 s +other Time = 0 s +rho Equations = 0.000175 s +U Equations = 0.001106 s +Y Equations = 0.00235904 s +E Equations = 0.000636 s +p Equations = 0.002081 s +calculate parcels = 34.386 s +chemistry correctThermo = 0.002737 s +turbulence correct = 0.001045 s +combustion correct(in Y) = 0.082076 s +percentage of chemistry = 88.8172 % +percentage of rho/U/Y/E = 4.62724 % +========Time details of each equation======= +rhoEqn Time = 0.000319 s +rhoEqn assamble = 0.000249 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001104 s +UEqn assamble = 0.000676 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000428 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00172 s +YEqn assamble = 0.000627 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000194 s +YEqn correct boundary = 0 s +EEqn Time = 0.000459 s +EEqn assamble = 0.000343 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 63.75 s ClockTime = 64 s +Courant Number mean: 0.000836189 max: 0.0176224 +Time = 0.0008275 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 14258 + Current mass in system = 1.25902e-09 + Linear momentum = (2.86986e-11 -1.06038e-08 0) + |Linear momentum| = 1.06038e-08 + Linear kinetic energy = 4.70933e-08 + model1: + number of parcels added = 14271 + mass introduced = 1.29338e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.15, 534.691 + Mass transfer phase change = 3.43545e-11 + D10, D32, Dmax (mu) = 49.8124, 82.3537, 149.883 + Liquid penetration 95% mass (m) = 0.00629513 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0049446, Final residual = 8.12794e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0109549, Final residual = 2.8136e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00195399, Final residual = 1.22759e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00244272, Final residual = 1.30731e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00275563, Final residual = 1.70073e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00275564, Final residual = 1.70213e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00192222, Final residual = 9.22738e-08, No Iterations 1 +min/max(T) = 617.399, 961.553 +GAMG: Solving for p, Initial residual = 0.0543867, Final residual = 0.000128244, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.80146e-06, global = 2.76385e-06, cumulative = 0.000790228 +GAMG: Solving for p, Initial residual = 0.000124322, Final residual = 8.77571e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.76584e-06, global = 2.76558e-06, cumulative = 0.000792993 +smoothSolver: Solving for epsilon, Initial residual = 0.000958552, Final residual = 1.43672e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00233532, Final residual = 3.73605e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100519 s +other Time = 1e-06 s +rho Equations = 0.000167 s +U Equations = 0.001071 s +Y Equations = 0.00265943 s +E Equations = 0.000698 s +p Equations = 0.003582 s +calculate parcels = 34.6118 s +chemistry correctThermo = 0.002798 s +turbulence correct = 0.001739 s +combustion correct(in Y) = 0.0875946 s +percentage of chemistry = 87.1423 % +percentage of rho/U/Y/E = 4.5717 % +========Time details of each equation======= +rhoEqn Time = 0.000505 s +rhoEqn assamble = 0.000388 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000117 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001069 s +UEqn assamble = 0.000647 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000422 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002018 s +YEqn assamble = 0.00074 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000229 s +YEqn correct boundary = 0 s +EEqn Time = 0.000502 s +EEqn assamble = 0.000382 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00012 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 64.08 s ClockTime = 65 s +Courant Number mean: 0.000845425 max: 0.0176157 +Time = 0.00083 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 45 new parcels + +Cloud: sprayCloud + Current number of parcels = 14303 + Current mass in system = 1.26177e-09 + Linear momentum = (2.98522e-11 -1.06164e-08 0) + |Linear momentum| = 1.06164e-08 + Linear kinetic energy = 4.70998e-08 + model1: + number of parcels added = 14316 + mass introduced = 1.29636e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.147, 533.578 + Mass transfer phase change = 3.45942e-11 + D10, D32, Dmax (mu) = 49.818, 82.3766, 149.889 + Liquid penetration 95% mass (m) = 0.00631153 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00500184, Final residual = 8.18791e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0108789, Final residual = 2.80602e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00193707, Final residual = 1.2043e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00244057, Final residual = 1.30323e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00275844, Final residual = 1.70547e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00275845, Final residual = 1.70687e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00192317, Final residual = 9.14776e-08, No Iterations 1 +min/max(T) = 617.702, 963.658 +GAMG: Solving for p, Initial residual = 0.0547821, Final residual = 0.000103132, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.79413e-06, global = 2.76036e-06, cumulative = 0.000795754 +GAMG: Solving for p, Initial residual = 9.9798e-05, Final residual = 7.64503e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.76282e-06, global = 2.76259e-06, cumulative = 0.000798516 +smoothSolver: Solving for epsilon, Initial residual = 0.000954996, Final residual = 1.42844e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00232566, Final residual = 3.71951e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.067201 s +other Time = 1e-06 s +rho Equations = 0.00016 s +U Equations = 0.000986 s +Y Equations = 0.00200355 s +E Equations = 0.000474 s +p Equations = 0.001632 s +calculate parcels = 34.7906 s +chemistry correctThermo = 0.00188 s +turbulence correct = 0.000911 s +combustion correct(in Y) = 0.0589715 s +percentage of chemistry = 87.7538 % +percentage of rho/U/Y/E = 5.39211 % +========Time details of each equation======= +rhoEqn Time = 0.000275 s +rhoEqn assamble = 0.000216 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000985 s +UEqn assamble = 0.000608 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000377 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00143 s +YEqn assamble = 0.000518 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000111 s +YEqn correct boundary = 0 s +EEqn Time = 0.000359 s +EEqn assamble = 0.000271 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 8.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 64.32 s ClockTime = 65 s +Courant Number mean: 0.000854642 max: 0.017613 +Time = 0.0008325 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 40 new parcels + +Cloud: sprayCloud + Current number of parcels = 14343 + Current mass in system = 1.26418e-09 + Linear momentum = (2.9757e-11 -1.06257e-08 0) + |Linear momentum| = 1.06257e-08 + Linear kinetic energy = 4.70902e-08 + model1: + number of parcels added = 14356 + mass introduced = 1.29901e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.153, 532.237 + Mass transfer phase change = 3.48347e-11 + D10, D32, Dmax (mu) = 49.7896, 82.406, 149.895 + Liquid penetration 95% mass (m) = 0.0063268 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00506441, Final residual = 8.20307e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0108038, Final residual = 2.79668e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00193323, Final residual = 1.20766e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00244196, Final residual = 1.30295e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00276183, Final residual = 1.71025e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00276183, Final residual = 1.71168e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0019271, Final residual = 9.10633e-08, No Iterations 1 +min/max(T) = 617.566, 965.796 +GAMG: Solving for p, Initial residual = 0.0552374, Final residual = 9.32351e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.80002e-06, global = 2.76954e-06, cumulative = 0.000801286 +GAMG: Solving for p, Initial residual = 8.95969e-05, Final residual = 5.26237e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.77178e-06, global = 2.77161e-06, cumulative = 0.000804057 +smoothSolver: Solving for epsilon, Initial residual = 0.000951645, Final residual = 1.42113e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00231645, Final residual = 3.70349e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.067321 s +other Time = 0 s +rho Equations = 0.000161 s +U Equations = 0.001012 s +Y Equations = 0.0020896 s +E Equations = 0.000478 s +p Equations = 0.001695 s +calculate parcels = 34.9823 s +chemistry correctThermo = 0.001967 s +turbulence correct = 0.000802 s +combustion correct(in Y) = 0.0589304 s +percentage of chemistry = 87.5364 % +percentage of rho/U/Y/E = 5.55636 % +========Time details of each equation======= +rhoEqn Time = 0.000286 s +rhoEqn assamble = 0.000227 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00101 s +UEqn assamble = 0.000643 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000367 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001535 s +YEqn assamble = 0.00055 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000144 s +YEqn correct boundary = 0 s +EEqn Time = 0.00036 s +EEqn assamble = 0.00027 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 64.58 s ClockTime = 65 s +Courant Number mean: 0.000863889 max: 0.0176036 +Time = 0.000835 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 63 new parcels + +Cloud: sprayCloud + Current number of parcels = 14406 + Current mass in system = 1.26809e-09 + Linear momentum = (2.83348e-11 -1.06499e-08 0) + |Linear momentum| = 1.06499e-08 + Linear kinetic energy = 4.71555e-08 + model1: + number of parcels added = 14419 + mass introduced = 1.30317e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.153, 530.674 + Mass transfer phase change = 3.5076e-11 + D10, D32, Dmax (mu) = 49.7225, 82.4333, 149.9 + Liquid penetration 95% mass (m) = 0.0063421 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00505549, Final residual = 8.17095e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0107342, Final residual = 2.78839e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00192405, Final residual = 1.19252e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00244333, Final residual = 1.30245e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00276514, Final residual = 1.71535e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00276515, Final residual = 1.71678e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00193069, Final residual = 9.08946e-08, No Iterations 1 +min/max(T) = 617.21, 967.967 +GAMG: Solving for p, Initial residual = 0.0558322, Final residual = 0.000127986, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.81672e-06, global = 2.77916e-06, cumulative = 0.000806837 +GAMG: Solving for p, Initial residual = 0.00012424, Final residual = 1.52448e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.78094e-06, global = 2.78089e-06, cumulative = 0.000809618 +smoothSolver: Solving for epsilon, Initial residual = 0.000947793, Final residual = 1.41313e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00230702, Final residual = 3.68637e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095317 s +other Time = 0 s +rho Equations = 0.000173 s +U Equations = 0.001082 s +Y Equations = 0.00236066 s +E Equations = 0.000599 s +p Equations = 0.002171 s +calculate parcels = 35.2124 s +chemistry correctThermo = 0.002784 s +turbulence correct = 0.001013 s +combustion correct(in Y) = 0.0849283 s +percentage of chemistry = 89.1009 % +percentage of rho/U/Y/E = 4.42173 % +========Time details of each equation======= +rhoEqn Time = 0.000307 s +rhoEqn assamble = 0.000241 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001081 s +UEqn assamble = 0.000659 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000422 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001689 s +YEqn assamble = 0.000622 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000156 s +YEqn correct boundary = 0 s +EEqn Time = 0.000443 s +EEqn assamble = 0.000331 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 64.91 s ClockTime = 65 s +Courant Number mean: 0.000873258 max: 0.0175918 +Time = 0.0008375 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 14454 + Current mass in system = 1.271e-09 + Linear momentum = (2.84168e-11 -1.06638e-08 0) + |Linear momentum| = 1.06638e-08 + Linear kinetic energy = 4.71679e-08 + model1: + number of parcels added = 14467 + mass introduced = 1.30632e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.141, 528.908 + Mass transfer phase change = 3.53179e-11 + D10, D32, Dmax (mu) = 49.7067, 82.4698, 149.906 + Liquid penetration 95% mass (m) = 0.0063581 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00500071, Final residual = 8.19738e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0106717, Final residual = 2.77319e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00191781, Final residual = 1.18315e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00244455, Final residual = 1.30195e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00276869, Final residual = 1.71969e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0027687, Final residual = 1.72113e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00193124, Final residual = 8.98677e-08, No Iterations 1 +min/max(T) = 616.857, 970.172 +GAMG: Solving for p, Initial residual = 0.0561194, Final residual = 0.000106556, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.82171e-06, global = 2.78764e-06, cumulative = 0.000812405 +GAMG: Solving for p, Initial residual = 0.000103556, Final residual = 8.33019e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.78938e-06, global = 2.78911e-06, cumulative = 0.000815194 +smoothSolver: Solving for epsilon, Initial residual = 0.000944269, Final residual = 1.40532e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00229696, Final residual = 3.66851e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.098902 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001129 s +Y Equations = 0.00236399 s +E Equations = 0.000606 s +p Equations = 0.001987 s +calculate parcels = 35.4532 s +chemistry correctThermo = 0.002811 s +turbulence correct = 0.001001 s +combustion correct(in Y) = 0.088635 s +percentage of chemistry = 89.619 % +percentage of rho/U/Y/E = 4.32346 % +========Time details of each equation======= +rhoEqn Time = 0.000319 s +rhoEqn assamble = 0.00025 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001128 s +UEqn assamble = 0.000688 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00044 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001717 s +YEqn assamble = 0.000633 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000168 s +YEqn correct boundary = 0 s +EEqn Time = 0.000452 s +EEqn assamble = 0.000339 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 65.25 s ClockTime = 66 s +Courant Number mean: 0.000882687 max: 0.0175797 +Time = 0.00084 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 58 new parcels + +Cloud: sprayCloud + Current number of parcels = 14512 + Current mass in system = 1.27452e-09 + Linear momentum = (2.91968e-11 -1.06834e-08 0) + |Linear momentum| = 1.06834e-08 + Linear kinetic energy = 4.72068e-08 + model1: + number of parcels added = 14525 + mass introduced = 1.31008e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.144, 526.94 + Mass transfer phase change = 3.55607e-11 + D10, D32, Dmax (mu) = 49.6847, 82.4982, 149.912 + Liquid penetration 95% mass (m) = 0.00637485 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00508393, Final residual = 8.3915e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0105861, Final residual = 2.75517e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00191433, Final residual = 1.20183e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00244623, Final residual = 1.30599e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00277229, Final residual = 1.72409e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0027723, Final residual = 1.72553e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.001936, Final residual = 9.0162e-08, No Iterations 1 +min/max(T) = 616.508, 972.411 +GAMG: Solving for p, Initial residual = 0.0565344, Final residual = 0.000108675, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.82868e-06, global = 2.79714e-06, cumulative = 0.000817991 +GAMG: Solving for p, Initial residual = 0.000105812, Final residual = 6.48047e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.79875e-06, global = 2.79855e-06, cumulative = 0.00082079 +smoothSolver: Solving for epsilon, Initial residual = 0.000941407, Final residual = 1.39771e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00228744, Final residual = 3.65123e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.099055 s +other Time = 1e-06 s +rho Equations = 0.000174 s +U Equations = 0.001267 s +Y Equations = 0.00239012 s +E Equations = 0.000602 s +p Equations = 0.002095 s +calculate parcels = 35.7012 s +chemistry correctThermo = 0.002789 s +turbulence correct = 0.001015 s +combustion correct(in Y) = 0.0885259 s +percentage of chemistry = 89.3704 % +percentage of rho/U/Y/E = 4.47542 % +========Time details of each equation======= +rhoEqn Time = 0.000321 s +rhoEqn assamble = 0.000253 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001266 s +UEqn assamble = 0.000748 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000518 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001658 s +YEqn assamble = 0.000635 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000138 s +YEqn correct boundary = 0 s +EEqn Time = 0.000451 s +EEqn assamble = 0.00033 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000121 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 65.6 s ClockTime = 66 s +Courant Number mean: 0.000892212 max: 0.0175792 +Time = 0.0008425 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 40 new parcels + +Cloud: sprayCloud + Current number of parcels = 14552 + Current mass in system = 1.27685e-09 + Linear momentum = (2.93569e-11 -1.06912e-08 0) + |Linear momentum| = 1.06912e-08 + Linear kinetic energy = 4.71865e-08 + model1: + number of parcels added = 14565 + mass introduced = 1.31265e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.157, 524.962 + Mass transfer phase change = 3.58043e-11 + D10, D32, Dmax (mu) = 49.6873, 82.5296, 149.918 + Liquid penetration 95% mass (m) = 0.00639046 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.005042, Final residual = 8.36892e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0105162, Final residual = 2.7379e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00190398, Final residual = 1.18263e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00244802, Final residual = 1.30792e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00277631, Final residual = 1.72777e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00277632, Final residual = 1.72922e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00193708, Final residual = 8.93182e-08, No Iterations 1 +min/max(T) = 616.169, 974.686 +GAMG: Solving for p, Initial residual = 0.0569134, Final residual = 0.000104799, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.83893e-06, global = 2.8055e-06, cumulative = 0.000823595 +GAMG: Solving for p, Initial residual = 0.000102521, Final residual = 9.62597e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.80753e-06, global = 2.80722e-06, cumulative = 0.000826403 +smoothSolver: Solving for epsilon, Initial residual = 0.000938332, Final residual = 1.39026e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00227859, Final residual = 3.63665e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092367 s +other Time = 0 s +rho Equations = 0.000181 s +U Equations = 0.001155 s +Y Equations = 0.00243485 s +E Equations = 0.000598 s +p Equations = 0.001992 s +calculate parcels = 35.9376 s +chemistry correctThermo = 0.002818 s +turbulence correct = 0.00096 s +combustion correct(in Y) = 0.0820311 s +percentage of chemistry = 88.81 % +percentage of rho/U/Y/E = 4.72988 % +========Time details of each equation======= +rhoEqn Time = 0.000324 s +rhoEqn assamble = 0.000256 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001154 s +UEqn assamble = 0.000698 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000456 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001735 s +YEqn assamble = 0.000651 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000153 s +YEqn correct boundary = 0 s +EEqn Time = 0.000443 s +EEqn assamble = 0.000329 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 65.91 s ClockTime = 66 s +Courant Number mean: 0.000901737 max: 0.0175671 +Time = 0.000845 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 14603 + Current mass in system = 1.27984e-09 + Linear momentum = (2.92974e-11 -1.0705e-08 0) + |Linear momentum| = 1.0705e-08 + Linear kinetic energy = 4.71945e-08 + model1: + number of parcels added = 14616 + mass introduced = 1.31589e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.144, 525.321 + Mass transfer phase change = 3.60488e-11 + D10, D32, Dmax (mu) = 49.4714, 82.5291, 149.924 + Liquid penetration 95% mass (m) = 0.00640743 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00514035, Final residual = 8.4018e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0104455, Final residual = 2.72411e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00189897, Final residual = 1.16698e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00245024, Final residual = 1.30831e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00277979, Final residual = 1.73171e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0027798, Final residual = 1.73316e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00194137, Final residual = 8.84662e-08, No Iterations 1 +min/max(T) = 615.84, 976.997 +GAMG: Solving for p, Initial residual = 0.0572855, Final residual = 0.000125398, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.85607e-06, global = 2.81664e-06, cumulative = 0.000829219 +GAMG: Solving for p, Initial residual = 0.000121393, Final residual = 1.58345e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.81864e-06, global = 2.81859e-06, cumulative = 0.000832038 +smoothSolver: Solving for epsilon, Initial residual = 0.000935039, Final residual = 1.38367e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00226948, Final residual = 3.62171e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.099965 s +other Time = 1e-06 s +rho Equations = 0.000236 s +U Equations = 0.00125 s +Y Equations = 0.00230798 s +E Equations = 0.000505 s +p Equations = 0.001909 s +calculate parcels = 36.1761 s +chemistry correctThermo = 0.002016 s +turbulence correct = 0.000848 s +combustion correct(in Y) = 0.090646 s +percentage of chemistry = 90.6778 % +percentage of rho/U/Y/E = 4.30048 % +========Time details of each equation======= +rhoEqn Time = 0.000373 s +rhoEqn assamble = 0.000278 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00125 s +UEqn assamble = 0.000761 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000489 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001545 s +YEqn assamble = 0.000569 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.4e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000385 s +EEqn assamble = 0.000287 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 66.26 s ClockTime = 67 s +Courant Number mean: 0.000911337 max: 0.0175474 +Time = 0.0008475 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 36 new parcels + +Cloud: sprayCloud + Current number of parcels = 14639 + Current mass in system = 1.28185e-09 + Linear momentum = (2.97341e-11 -1.07094e-08 0) + |Linear momentum| = 1.07094e-08 + Linear kinetic energy = 4.71559e-08 + model1: + number of parcels added = 14652 + mass introduced = 1.31815e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.141, 525.634 + Mass transfer phase change = 3.62942e-11 + D10, D32, Dmax (mu) = 49.4492, 82.5588, 149.93 + Liquid penetration 95% mass (m) = 0.00642224 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00506833, Final residual = 8.22624e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0104119, Final residual = 2.71366e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00188957, Final residual = 1.15238e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00245249, Final residual = 1.3122e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00278409, Final residual = 1.7358e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0027841, Final residual = 1.73725e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00194051, Final residual = 8.74198e-08, No Iterations 1 +min/max(T) = 615.534, 979.346 +GAMG: Solving for p, Initial residual = 0.0574354, Final residual = 0.00010543, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.85988e-06, global = 2.82602e-06, cumulative = 0.000834864 +GAMG: Solving for p, Initial residual = 0.000102141, Final residual = 1.42602e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.82778e-06, global = 2.82774e-06, cumulative = 0.000837692 +smoothSolver: Solving for epsilon, Initial residual = 0.000931472, Final residual = 1.37551e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00226, Final residual = 3.60492e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097805 s +other Time = 1e-06 s +rho Equations = 0.000177 s +U Equations = 0.001134 s +Y Equations = 0.00237901 s +E Equations = 0.000629 s +p Equations = 0.002205 s +calculate parcels = 36.4087 s +chemistry correctThermo = 0.002809 s +turbulence correct = 0.000992 s +combustion correct(in Y) = 0.087267 s +percentage of chemistry = 89.2255 % +percentage of rho/U/Y/E = 4.41593 % +========Time details of each equation======= +rhoEqn Time = 0.000318 s +rhoEqn assamble = 0.000253 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001132 s +UEqn assamble = 0.000698 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000434 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001717 s +YEqn assamble = 0.000647 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000164 s +YEqn correct boundary = 0 s +EEqn Time = 0.000473 s +EEqn assamble = 0.000355 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 66.59 s ClockTime = 67 s +Courant Number mean: 0.000920899 max: 0.017513 +Time = 0.00085 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 55 new parcels + +Cloud: sprayCloud + Current number of parcels = 14694 + Current mass in system = 1.285e-09 + Linear momentum = (2.97625e-11 -1.07241e-08 0) + |Linear momentum| = 1.07241e-08 + Linear kinetic energy = 4.71654e-08 + model1: + number of parcels added = 14707 + mass introduced = 1.32154e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.152, 525.909 + Mass transfer phase change = 3.65404e-11 + D10, D32, Dmax (mu) = 49.4441, 82.5871, 149.936 + Liquid penetration 95% mass (m) = 0.00643775 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00509001, Final residual = 8.20597e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0103555, Final residual = 2.70331e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0018826, Final residual = 1.14489e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00245478, Final residual = 1.31484e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00278811, Final residual = 1.73966e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00278811, Final residual = 1.74113e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00194152, Final residual = 8.67631e-08, No Iterations 1 +min/max(T) = 615.242, 981.732 +GAMG: Solving for p, Initial residual = 0.0577212, Final residual = 9.50827e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.86826e-06, global = 2.83579e-06, cumulative = 0.000840527 +GAMG: Solving for p, Initial residual = 9.11226e-05, Final residual = 8.05932e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.83777e-06, global = 2.83748e-06, cumulative = 0.000843365 +smoothSolver: Solving for epsilon, Initial residual = 0.000929631, Final residual = 1.36804e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0022515, Final residual = 3.58917e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.073793 s +other Time = 1e-06 s +rho Equations = 0.000204 s +U Equations = 0.00128 s +Y Equations = 0.00280957 s +E Equations = 0.000695 s +p Equations = 0.002699 s +calculate parcels = 36.6073 s +chemistry correctThermo = 0.002099 s +turbulence correct = 0.001037 s +combustion correct(in Y) = 0.0627264 s +percentage of chemistry = 85.0032 % +percentage of rho/U/Y/E = 6.76023 % +========Time details of each equation======= +rhoEqn Time = 0.000364 s +rhoEqn assamble = 0.000289 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001279 s +UEqn assamble = 0.000858 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000421 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00215 s +YEqn assamble = 0.000713 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000257 s +YEqn correct boundary = 0 s +EEqn Time = 0.000522 s +EEqn assamble = 0.000406 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 66.87 s ClockTime = 67 s +Courant Number mean: 0.000930502 max: 0.0174861 +Time = 0.0008525 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 53 new parcels + +Cloud: sprayCloud + Current number of parcels = 14747 + Current mass in system = 1.28799e-09 + Linear momentum = (2.91113e-11 -1.07371e-08 0) + |Linear momentum| = 1.07372e-08 + Linear kinetic energy = 4.71655e-08 + model1: + number of parcels added = 14760 + mass introduced = 1.32478e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.138, 526.135 + Mass transfer phase change = 3.67873e-11 + D10, D32, Dmax (mu) = 49.4136, 82.6105, 149.942 + Liquid penetration 95% mass (m) = 0.00645353 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00507085, Final residual = 8.1572e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0103352, Final residual = 2.71325e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00186945, Final residual = 1.13388e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00245733, Final residual = 1.31657e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00279288, Final residual = 1.74383e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00279289, Final residual = 1.74531e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00193891, Final residual = 8.66505e-08, No Iterations 1 +min/max(T) = 614.964, 984.157 +GAMG: Solving for p, Initial residual = 0.0579182, Final residual = 9.73894e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.87695e-06, global = 2.8453e-06, cumulative = 0.00084621 +GAMG: Solving for p, Initial residual = 9.20127e-05, Final residual = 9.68572e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.84702e-06, global = 2.84669e-06, cumulative = 0.000849057 +smoothSolver: Solving for epsilon, Initial residual = 0.000928084, Final residual = 1.36099e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0022425, Final residual = 3.57239e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.093755 s +other Time = 0 s +rho Equations = 0.000198 s +U Equations = 0.001127 s +Y Equations = 0.00250125 s +E Equations = 0.000593 s +p Equations = 0.002037 s +calculate parcels = 36.8009 s +chemistry correctThermo = 0.00277 s +turbulence correct = 0.001069 s +combustion correct(in Y) = 0.0832618 s +percentage of chemistry = 88.8078 % +percentage of rho/U/Y/E = 4.71361 % +========Time details of each equation======= +rhoEqn Time = 0.000341 s +rhoEqn assamble = 0.00027 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001127 s +UEqn assamble = 0.000679 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000448 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001851 s +YEqn assamble = 0.000652 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000186 s +YEqn correct boundary = 0 s +EEqn Time = 0.000438 s +EEqn assamble = 0.000328 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00011 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 67.15 s ClockTime = 68 s +Courant Number mean: 0.000940205 max: 0.0174551 +Time = 0.000855 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 42 new parcels + +Cloud: sprayCloud + Current number of parcels = 14789 + Current mass in system = 1.29028e-09 + Linear momentum = (2.90433e-11 -1.07435e-08 0) + |Linear momentum| = 1.07435e-08 + Linear kinetic energy = 4.71338e-08 + model1: + number of parcels added = 14802 + mass introduced = 1.32732e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.155, 526.247 + Mass transfer phase change = 3.70351e-11 + D10, D32, Dmax (mu) = 49.3453, 82.6332, 149.948 + Liquid penetration 95% mass (m) = 0.00646977 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00518093, Final residual = 8.45055e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0103261, Final residual = 2.7164e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00186664, Final residual = 1.11777e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00245969, Final residual = 1.31847e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00279761, Final residual = 1.74868e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00279761, Final residual = 1.75017e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00194093, Final residual = 8.68916e-08, No Iterations 1 +min/max(T) = 614.698, 986.622 +GAMG: Solving for p, Initial residual = 0.0582853, Final residual = 0.00010921, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.88988e-06, global = 2.85379e-06, cumulative = 0.000851911 +GAMG: Solving for p, Initial residual = 0.000105353, Final residual = 9.05135e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.8558e-06, global = 2.85547e-06, cumulative = 0.000854766 +smoothSolver: Solving for epsilon, Initial residual = 0.000926869, Final residual = 1.35553e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00223404, Final residual = 3.55665e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.099098 s +other Time = 0 s +rho Equations = 0.000173 s +U Equations = 0.001168 s +Y Equations = 0.00352803 s +E Equations = 0.000954 s +p Equations = 0.003258 s +calculate parcels = 37.0404 s +chemistry correctThermo = 0.005358 s +turbulence correct = 0.001573 s +combustion correct(in Y) = 0.082821 s +percentage of chemistry = 83.5748 % +percentage of rho/U/Y/E = 5.87603 % +========Time details of each equation======= +rhoEqn Time = 0.000437 s +rhoEqn assamble = 0.000329 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000108 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001167 s +UEqn assamble = 0.000717 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00045 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002815 s +YEqn assamble = 0.001033 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00051 s +YEqn correct boundary = 0 s +EEqn Time = 0.000721 s +EEqn assamble = 0.000525 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000196 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 67.49 s ClockTime = 68 s +Courant Number mean: 0.000950006 max: 0.0174441 +Time = 0.0008575 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 45 new parcels + +Cloud: sprayCloud + Current number of parcels = 14834 + Current mass in system = 1.29271e-09 + Linear momentum = (2.8746e-11 -1.07509e-08 0) + |Linear momentum| = 1.07509e-08 + Linear kinetic energy = 4.71058e-08 + model1: + number of parcels added = 14847 + mass introduced = 1.33e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.14, 526.242 + Mass transfer phase change = 3.72837e-11 + D10, D32, Dmax (mu) = 48.4693, 82.631, 149.954 + Liquid penetration 95% mass (m) = 0.00648452 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00529492, Final residual = 8.4427e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0103063, Final residual = 2.72111e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0018758, Final residual = 1.1081e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00246251, Final residual = 1.32546e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00280232, Final residual = 1.75387e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00280232, Final residual = 1.75537e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00194727, Final residual = 8.71764e-08, No Iterations 1 +min/max(T) = 614.452, 989.127 +GAMG: Solving for p, Initial residual = 0.0585035, Final residual = 0.000111549, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.89824e-06, global = 2.86405e-06, cumulative = 0.00085763 +GAMG: Solving for p, Initial residual = 0.000106488, Final residual = 1.62472e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.86582e-06, global = 2.86576e-06, cumulative = 0.000860496 +smoothSolver: Solving for epsilon, Initial residual = 0.000925761, Final residual = 1.35118e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0022259, Final residual = 3.54031e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100406 s +other Time = 0 s +rho Equations = 0.000192 s +U Equations = 0.001085 s +Y Equations = 0.00229743 s +E Equations = 0.000498 s +p Equations = 0.00258 s +calculate parcels = 37.2764 s +chemistry correctThermo = 0.002256 s +turbulence correct = 0.001092 s +combustion correct(in Y) = 0.0902036 s +percentage of chemistry = 89.8388 % +percentage of rho/U/Y/E = 4.05596 % +========Time details of each equation======= +rhoEqn Time = 0.000357 s +rhoEqn assamble = 0.000283 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001085 s +UEqn assamble = 0.000661 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000424 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001657 s +YEqn assamble = 0.000629 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000112 s +YEqn correct boundary = 0 s +EEqn Time = 0.000374 s +EEqn assamble = 0.00028 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 67.83 s ClockTime = 68 s +Courant Number mean: 0.000959983 max: 0.0174433 +Time = 0.00086 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 14883 + Current mass in system = 1.29534e-09 + Linear momentum = (2.89054e-11 -1.07598e-08 0) + |Linear momentum| = 1.07598e-08 + Linear kinetic energy = 4.7084e-08 + model1: + number of parcels added = 14896 + mass introduced = 1.33288e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.132, 526.126 + Mass transfer phase change = 3.75331e-11 + D10, D32, Dmax (mu) = 48.4787, 82.6789, 149.96 + Liquid penetration 95% mass (m) = 0.00649911 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00526291, Final residual = 8.41485e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0103113, Final residual = 2.7264e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00187422, Final residual = 1.10579e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0024652, Final residual = 1.32963e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00280737, Final residual = 1.75797e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00280737, Final residual = 1.75947e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00194641, Final residual = 8.68336e-08, No Iterations 1 +min/max(T) = 614.237, 991.674 +GAMG: Solving for p, Initial residual = 0.0587169, Final residual = 0.000112307, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.91054e-06, global = 2.87183e-06, cumulative = 0.000863368 +GAMG: Solving for p, Initial residual = 0.000107808, Final residual = 2.00538e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.87405e-06, global = 2.87398e-06, cumulative = 0.000866242 +smoothSolver: Solving for epsilon, Initial residual = 0.00092416, Final residual = 1.34615e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00221738, Final residual = 3.52264e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.099016 s +other Time = 0 s +rho Equations = 0.000172 s +U Equations = 0.001113 s +Y Equations = 0.00245309 s +E Equations = 0.000606 s +p Equations = 0.002315 s +calculate parcels = 37.5315 s +chemistry correctThermo = 0.002769 s +turbulence correct = 0.000989 s +combustion correct(in Y) = 0.0884049 s +percentage of chemistry = 89.2835 % +percentage of rho/U/Y/E = 4.38726 % +========Time details of each equation======= +rhoEqn Time = 0.000335 s +rhoEqn assamble = 0.000268 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001113 s +UEqn assamble = 0.00067 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000443 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001797 s +YEqn assamble = 0.000662 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000175 s +YEqn correct boundary = 0 s +EEqn Time = 0.000451 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 68.18 s ClockTime = 69 s +Courant Number mean: 0.00097006 max: 0.0174191 +Time = 0.0008625 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 60 new parcels + +Cloud: sprayCloud + Current number of parcels = 14943 + Current mass in system = 1.29857e-09 + Linear momentum = (2.94181e-11 -1.07738e-08 0) + |Linear momentum| = 1.07738e-08 + Linear kinetic energy = 4.70841e-08 + model1: + number of parcels added = 14956 + mass introduced = 1.33636e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.134, 525.906 + Mass transfer phase change = 3.77832e-11 + D10, D32, Dmax (mu) = 48.4829, 82.7104, 149.966 + Liquid penetration 95% mass (m) = 0.00651413 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00541936, Final residual = 8.57054e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0103041, Final residual = 2.7297e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00187218, Final residual = 1.10796e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00246826, Final residual = 1.33411e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0028125, Final residual = 1.76197e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00281251, Final residual = 1.76346e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00194506, Final residual = 8.63308e-08, No Iterations 1 +min/max(T) = 614.044, 994.263 +GAMG: Solving for p, Initial residual = 0.0590133, Final residual = 0.000107782, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.91811e-06, global = 2.87996e-06, cumulative = 0.000869122 +GAMG: Solving for p, Initial residual = 0.000102357, Final residual = 9.45994e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.8828e-06, global = 2.88246e-06, cumulative = 0.000872004 +smoothSolver: Solving for epsilon, Initial residual = 0.000922536, Final residual = 1.34141e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00220872, Final residual = 3.50862e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094394 s +other Time = 1e-06 s +rho Equations = 0.000173 s +U Equations = 0.001115 s +Y Equations = 0.0020878 s +E Equations = 0.000489 s +p Equations = 0.0017 s +calculate parcels = 37.7863 s +chemistry correctThermo = 0.002022 s +turbulence correct = 0.000882 s +combustion correct(in Y) = 0.0857252 s +percentage of chemistry = 90.8164 % +percentage of rho/U/Y/E = 4.09433 % +========Time details of each equation======= +rhoEqn Time = 0.000293 s +rhoEqn assamble = 0.000235 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001114 s +UEqn assamble = 0.000679 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000435 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00142 s +YEqn assamble = 0.000536 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.00037 s +EEqn assamble = 0.000278 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 68.53 s ClockTime = 69 s +Courant Number mean: 0.000980299 max: 0.017391 +Time = 0.000865 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 55 new parcels + +Cloud: sprayCloud + Current number of parcels = 14997 + Current mass in system = 1.30149e-09 + Linear momentum = (2.91684e-11 -1.07848e-08 0) + |Linear momentum| = 1.07848e-08 + Linear kinetic energy = 4.70693e-08 + model1: + number of parcels added = 15011 + mass introduced = 1.33952e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.134, 525.58 + Mass transfer phase change = 3.80348e-11 + D10, D32, Dmax (mu) = 49.4575, 82.712, 149.972 + Liquid penetration 95% mass (m) = 0.00653015 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00550778, Final residual = 8.63573e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.010337, Final residual = 2.74591e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00187865, Final residual = 1.09646e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00247351, Final residual = 1.34218e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00281776, Final residual = 1.76674e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00281776, Final residual = 1.76823e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00195124, Final residual = 8.65294e-08, No Iterations 1 +min/max(T) = 613.872, 996.895 +GAMG: Solving for p, Initial residual = 0.0591169, Final residual = 0.000111331, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.93637e-06, global = 2.89786e-06, cumulative = 0.000874902 +GAMG: Solving for p, Initial residual = 0.000106905, Final residual = 1.99602e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.90031e-06, global = 2.90024e-06, cumulative = 0.000877802 +smoothSolver: Solving for epsilon, Initial residual = 0.000921488, Final residual = 1.3372e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00220073, Final residual = 3.49783e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.098828 s +other Time = 0 s +rho Equations = 0.000169 s +U Equations = 0.001178 s +Y Equations = 0.00249693 s +E Equations = 0.000601 s +p Equations = 0.002201 s +calculate parcels = 38.0234 s +chemistry correctThermo = 0.002819 s +turbulence correct = 0.001051 s +combustion correct(in Y) = 0.0881121 s +percentage of chemistry = 89.157 % +percentage of rho/U/Y/E = 4.49764 % +========Time details of each equation======= +rhoEqn Time = 0.000308 s +rhoEqn assamble = 0.000243 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001178 s +UEqn assamble = 0.000733 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000445 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001665 s +YEqn assamble = 0.000647 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000101 s +YEqn correct boundary = 0 s +EEqn Time = 0.000448 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 68.87 s ClockTime = 69 s +Courant Number mean: 0.000990776 max: 0.0173718 +Time = 0.0008675 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 15046 + Current mass in system = 1.30403e-09 + Linear momentum = (2.88412e-11 -1.07923e-08 0) + |Linear momentum| = 1.07923e-08 + Linear kinetic energy = 4.70386e-08 + model1: + number of parcels added = 15060 + mass introduced = 1.34232e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.13, 525.135 + Mass transfer phase change = 3.8286e-11 + D10, D32, Dmax (mu) = 49.4368, 82.7319, 149.984 + Liquid penetration 95% mass (m) = 0.00654558 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00542227, Final residual = 8.54824e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.01039, Final residual = 2.76775e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00187868, Final residual = 1.08112e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00247394, Final residual = 1.33798e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00282338, Final residual = 1.7723e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00282338, Final residual = 1.7738e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00195172, Final residual = 8.57538e-08, No Iterations 1 +min/max(T) = 613.728, 999.572 +GAMG: Solving for p, Initial residual = 0.0592482, Final residual = 0.000101345, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.93038e-06, global = 2.89284e-06, cumulative = 0.000880695 +GAMG: Solving for p, Initial residual = 9.799e-05, Final residual = 2.35766e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.89502e-06, global = 2.89493e-06, cumulative = 0.00088359 +smoothSolver: Solving for epsilon, Initial residual = 0.000919862, Final residual = 1.33222e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00219225, Final residual = 3.48562e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.070888 s +other Time = 0 s +rho Equations = 0.000169 s +U Equations = 0.001004 s +Y Equations = 0.00269318 s +E Equations = 0.000568 s +p Equations = 0.001887 s +calculate parcels = 38.2658 s +chemistry correctThermo = 0.001983 s +turbulence correct = 0.00085 s +combustion correct(in Y) = 0.0615398 s +percentage of chemistry = 86.8127 % +percentage of rho/U/Y/E = 6.25519 % +========Time details of each equation======= +rhoEqn Time = 0.000304 s +rhoEqn assamble = 0.000233 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001004 s +UEqn assamble = 0.000638 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000366 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002128 s +YEqn assamble = 0.000623 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000325 s +YEqn correct boundary = 0 s +EEqn Time = 0.000439 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000103 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 69.18 s ClockTime = 70 s +Courant Number mean: 0.00100135 max: 0.0173604 +Time = 0.00087 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 58 new parcels + +Cloud: sprayCloud + Current number of parcels = 15104 + Current mass in system = 1.30704e-09 + Linear momentum = (2.92839e-11 -1.08036e-08 0) + |Linear momentum| = 1.08036e-08 + Linear kinetic energy = 4.70234e-08 + model1: + number of parcels added = 15118 + mass introduced = 1.34558e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.13, 527.111 + Mass transfer phase change = 3.85378e-11 + D10, D32, Dmax (mu) = 49.4531, 82.7574, 149.994 + Liquid penetration 95% mass (m) = 0.00656102 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00557671, Final residual = 8.8001e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0104173, Final residual = 2.7884e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00187054, Final residual = 1.06653e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00247736, Final residual = 1.34258e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00282883, Final residual = 1.77676e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00282883, Final residual = 1.77826e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00195267, Final residual = 8.53241e-08, No Iterations 1 +min/max(T) = 613.605, 1002.29 +GAMG: Solving for p, Initial residual = 0.0595257, Final residual = 8.37033e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.93155e-06, global = 2.90088e-06, cumulative = 0.000886491 +GAMG: Solving for p, Initial residual = 8.01894e-05, Final residual = 7.88036e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.90348e-06, global = 2.90317e-06, cumulative = 0.000889394 +smoothSolver: Solving for epsilon, Initial residual = 0.000918344, Final residual = 1.32772e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0021843, Final residual = 3.47491e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.073442 s +other Time = 0 s +rho Equations = 0.000165 s +U Equations = 0.001014 s +Y Equations = 0.00207849 s +E Equations = 0.000484 s +p Equations = 0.001668 s +calculate parcels = 38.4504 s +chemistry correctThermo = 0.001953 s +turbulence correct = 0.000815 s +combustion correct(in Y) = 0.0650865 s +percentage of chemistry = 88.623 % +percentage of rho/U/Y/E = 5.09449 % +========Time details of each equation======= +rhoEqn Time = 0.000283 s +rhoEqn assamble = 0.000225 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001014 s +UEqn assamble = 0.000639 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000375 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001514 s +YEqn assamble = 0.000551 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000146 s +YEqn correct boundary = 0 s +EEqn Time = 0.000365 s +EEqn assamble = 0.000272 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 69.44 s ClockTime = 70 s +Courant Number mean: 0.00101214 max: 0.0173471 +Time = 0.0008725 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 39 new parcels + +Cloud: sprayCloud + Current number of parcels = 15143 + Current mass in system = 1.30897e-09 + Linear momentum = (2.88307e-11 -1.08055e-08 0) + |Linear momentum| = 1.08055e-08 + Linear kinetic energy = 4.69676e-08 + model1: + number of parcels added = 15157 + mass introduced = 1.34776e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.131, 528.997 + Mass transfer phase change = 3.87903e-11 + D10, D32, Dmax (mu) = 49.4551, 82.776, 150.003 + Liquid penetration 95% mass (m) = 0.00657634 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0056452, Final residual = 8.79538e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0104461, Final residual = 2.80666e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00186726, Final residual = 1.06009e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00248073, Final residual = 1.34291e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00283478, Final residual = 1.78161e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00283478, Final residual = 1.78312e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00195208, Final residual = 8.49003e-08, No Iterations 1 +min/max(T) = 613.503, 1005.06 +GAMG: Solving for p, Initial residual = 0.0596183, Final residual = 7.28171e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.93746e-06, global = 2.90709e-06, cumulative = 0.000892301 +GAMG: Solving for p, Initial residual = 6.95208e-05, Final residual = 8.1297e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.91018e-06, global = 2.90984e-06, cumulative = 0.000895211 +smoothSolver: Solving for epsilon, Initial residual = 0.000916618, Final residual = 1.32308e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00217626, Final residual = 3.46397e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.093103 s +other Time = 0 s +rho Equations = 0.000237 s +U Equations = 0.001205 s +Y Equations = 0.00238797 s +E Equations = 0.000656 s +p Equations = 0.002003 s +calculate parcels = 38.708 s +chemistry correctThermo = 0.002785 s +turbulence correct = 0.001029 s +combustion correct(in Y) = 0.08257 s +percentage of chemistry = 88.6868 % +percentage of rho/U/Y/E = 4.81828 % +========Time details of each equation======= +rhoEqn Time = 0.000379 s +rhoEqn assamble = 0.000304 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001204 s +UEqn assamble = 0.000752 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000452 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001735 s +YEqn assamble = 0.00064 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000175 s +YEqn correct boundary = 0 s +EEqn Time = 0.000476 s +EEqn assamble = 0.000355 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000121 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 69.79 s ClockTime = 70 s +Courant Number mean: 0.00102313 max: 0.0173319 +Time = 0.000875 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 59 new parcels + +Cloud: sprayCloud + Current number of parcels = 15201 + Current mass in system = 1.31195e-09 + Linear momentum = (2.83718e-11 -1.08161e-08 0) + |Linear momentum| = 1.08161e-08 + Linear kinetic energy = 4.69474e-08 + model1: + number of parcels added = 15216 + mass introduced = 1.35099e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.138, 530.66 + Mass transfer phase change = 3.90443e-11 + D10, D32, Dmax (mu) = 49.9414, 82.8087, 150.013 + Liquid penetration 95% mass (m) = 0.00659229 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00576733, Final residual = 8.96889e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0104965, Final residual = 2.82938e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00186262, Final residual = 1.07208e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00248645, Final residual = 1.35012e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00284063, Final residual = 1.78605e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00284063, Final residual = 1.78756e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00195488, Final residual = 8.54164e-08, No Iterations 1 +min/max(T) = 613.421, 1007.88 +GAMG: Solving for p, Initial residual = 0.0598485, Final residual = 9.11533e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.95988e-06, global = 2.92546e-06, cumulative = 0.000898137 +GAMG: Solving for p, Initial residual = 8.66291e-05, Final residual = 8.7127e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.92835e-06, global = 2.92802e-06, cumulative = 0.000901065 +smoothSolver: Solving for epsilon, Initial residual = 0.000914724, Final residual = 1.31771e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00216797, Final residual = 3.4522e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.087428 s +other Time = 1e-06 s +rho Equations = 0.00017 s +U Equations = 0.001097 s +Y Equations = 0.00203935 s +E Equations = 0.000492 s +p Equations = 0.001622 s +calculate parcels = 38.9618 s +chemistry correctThermo = 0.002002 s +turbulence correct = 0.000792 s +combustion correct(in Y) = 0.0790216 s +percentage of chemistry = 90.3848 % +percentage of rho/U/Y/E = 4.34455 % +========Time details of each equation======= +rhoEqn Time = 0.000282 s +rhoEqn assamble = 0.000222 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001096 s +UEqn assamble = 0.000664 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000432 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00141 s +YEqn assamble = 0.000527 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.5e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000375 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 70.13 s ClockTime = 71 s +Courant Number mean: 0.00103437 max: 0.0173105 +Time = 0.0008775 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 15248 + Current mass in system = 1.31431e-09 + Linear momentum = (2.82108e-11 -1.08213e-08 0) + |Linear momentum| = 1.08213e-08 + Linear kinetic energy = 4.69049e-08 + model1: + number of parcels added = 15264 + mass introduced = 1.3536e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.132, 531.493 + Mass transfer phase change = 3.92987e-11 + D10, D32, Dmax (mu) = 50.7578, 82.8322, 150.022 + Liquid penetration 95% mass (m) = 0.00660829 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00582604, Final residual = 9.22821e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0105734, Final residual = 2.85494e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00187291, Final residual = 1.06451e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00248953, Final residual = 1.35902e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00284687, Final residual = 1.79087e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00284687, Final residual = 1.79238e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00195729, Final residual = 8.56733e-08, No Iterations 1 +min/max(T) = 613.346, 1010.74 +GAMG: Solving for p, Initial residual = 0.0600587, Final residual = 9.6631e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.96442e-06, global = 2.92969e-06, cumulative = 0.000903994 +GAMG: Solving for p, Initial residual = 9.26843e-05, Final residual = 7.65768e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.93258e-06, global = 2.9323e-06, cumulative = 0.000906927 +smoothSolver: Solving for epsilon, Initial residual = 0.000913616, Final residual = 1.3145e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00216065, Final residual = 3.44208e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.090368 s +other Time = 0 s +rho Equations = 0.000172 s +U Equations = 0.001226 s +Y Equations = 0.00247155 s +E Equations = 0.00061 s +p Equations = 0.002068 s +calculate parcels = 39.2263 s +chemistry correctThermo = 0.002795 s +turbulence correct = 0.001049 s +combustion correct(in Y) = 0.0797735 s +percentage of chemistry = 88.2762 % +percentage of rho/U/Y/E = 4.95701 % +========Time details of each equation======= +rhoEqn Time = 0.000316 s +rhoEqn assamble = 0.000249 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001225 s +UEqn assamble = 0.000756 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000469 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001809 s +YEqn assamble = 0.000659 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000181 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 70.49 s ClockTime = 71 s +Courant Number mean: 0.00104591 max: 0.0173124 +Time = 0.00088 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 43 new parcels + +Cloud: sprayCloud + Current number of parcels = 15291 + Current mass in system = 1.31637e-09 + Linear momentum = (2.82282e-11 -1.08241e-08 0) + |Linear momentum| = 1.08242e-08 + Linear kinetic energy = 4.68524e-08 + model1: + number of parcels added = 15307 + mass introduced = 1.35593e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.13, 531.888 + Mass transfer phase change = 3.95525e-11 + D10, D32, Dmax (mu) = 50.7715, 82.8696, 150.032 + Liquid penetration 95% mass (m) = 0.00662424 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00592008, Final residual = 9.31034e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0106468, Final residual = 2.88996e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00185861, Final residual = 1.03503e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00249053, Final residual = 1.35918e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00285345, Final residual = 1.79745e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00285345, Final residual = 1.79896e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00195486, Final residual = 8.53891e-08, No Iterations 1 +min/max(T) = 613.285, 1013.66 +GAMG: Solving for p, Initial residual = 0.0601662, Final residual = 0.000106623, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.9664e-06, global = 2.92141e-06, cumulative = 0.000909848 +GAMG: Solving for p, Initial residual = 0.000102042, Final residual = 1.98689e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.92499e-06, global = 2.92491e-06, cumulative = 0.000912773 +smoothSolver: Solving for epsilon, Initial residual = 0.00091168, Final residual = 1.30943e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00215312, Final residual = 3.43369e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09064 s +other Time = 0 s +rho Equations = 0.000174 s +U Equations = 0.001284 s +Y Equations = 0.00211244 s +E Equations = 0.000491 s +p Equations = 0.001823 s +calculate parcels = 39.4788 s +chemistry correctThermo = 0.001989 s +turbulence correct = 0.000871 s +combustion correct(in Y) = 0.0816976 s +percentage of chemistry = 90.1341 % +percentage of rho/U/Y/E = 4.48085 % +========Time details of each equation======= +rhoEqn Time = 0.000291 s +rhoEqn assamble = 0.00023 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001283 s +UEqn assamble = 0.000806 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000477 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001373 s +YEqn assamble = 0.00053 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 4.5e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000371 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 70.83 s ClockTime = 71 s +Courant Number mean: 0.00105767 max: 0.017317 +Time = 0.0008825 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 15339 + Current mass in system = 1.31868e-09 + Linear momentum = (2.83012e-11 -1.08289e-08 0) + |Linear momentum| = 1.08289e-08 + Linear kinetic energy = 4.68078e-08 + model1: + number of parcels added = 15355 + mass introduced = 1.35849e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.124, 532.193 + Mass transfer phase change = 3.98069e-11 + D10, D32, Dmax (mu) = 50.7805, 82.893, 150.042 + Liquid penetration 95% mass (m) = 0.00663867 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00622045, Final residual = 9.63084e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0107129, Final residual = 2.9144e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00186022, Final residual = 1.03117e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00249494, Final residual = 1.36039e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00286025, Final residual = 1.80422e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00286025, Final residual = 1.80576e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00195899, Final residual = 8.59526e-08, No Iterations 1 +min/max(T) = 613.247, 1016.62 +GAMG: Solving for p, Initial residual = 0.0602357, Final residual = 9.58456e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.96934e-06, global = 2.9284e-06, cumulative = 0.000915701 +GAMG: Solving for p, Initial residual = 9.07523e-05, Final residual = 9.40392e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.93223e-06, global = 2.93184e-06, cumulative = 0.000918633 +smoothSolver: Solving for epsilon, Initial residual = 0.000909833, Final residual = 1.30406e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00214592, Final residual = 3.42801e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.08341 s +other Time = 0 s +rho Equations = 0.000152 s +U Equations = 0.000952 s +Y Equations = 0.00198586 s +E Equations = 0.000521 s +p Equations = 0.003453 s +calculate parcels = 39.7096 s +chemistry correctThermo = 0.005001 s +turbulence correct = 0.001635 s +combustion correct(in Y) = 0.0695071 s +percentage of chemistry = 83.3319 % +percentage of rho/U/Y/E = 4.32905 % +========Time details of each equation======= +rhoEqn Time = 0.000437 s +rhoEqn assamble = 0.000329 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000108 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000952 s +UEqn assamble = 0.000583 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000369 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001433 s +YEqn assamble = 0.000539 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000137 s +YEqn correct boundary = 0 s +EEqn Time = 0.000403 s +EEqn assamble = 0.000305 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 71.14 s ClockTime = 72 s +Courant Number mean: 0.00106975 max: 0.0173124 +Time = 0.000885 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 15390 + Current mass in system = 1.32113e-09 + Linear momentum = (2.83138e-11 -1.08347e-08 0) + |Linear momentum| = 1.08347e-08 + Linear kinetic energy = 4.67673e-08 + model1: + number of parcels added = 15406 + mass introduced = 1.36119e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.122, 532.417 + Mass transfer phase change = 4.00618e-11 + D10, D32, Dmax (mu) = 50.7797, 82.9209, 150.051 + Liquid penetration 95% mass (m) = 0.00665483 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00630783, Final residual = 9.77035e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0108055, Final residual = 2.94554e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00185795, Final residual = 1.03831e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00250168, Final residual = 1.37177e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00287089, Final residual = 1.81585e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00287089, Final residual = 1.81741e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196083, Final residual = 8.6999e-08, No Iterations 1 +min/max(T) = 613.233, 1019.64 +GAMG: Solving for p, Initial residual = 0.0604101, Final residual = 0.000150587, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.99598e-06, global = 2.93418e-06, cumulative = 0.000921567 +GAMG: Solving for p, Initial residual = 0.000142849, Final residual = 3.48142e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.93815e-06, global = 2.93802e-06, cumulative = 0.000924505 +smoothSolver: Solving for epsilon, Initial residual = 0.000908197, Final residual = 1.29876e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00213896, Final residual = 3.42325e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.090255 s +other Time = 0 s +rho Equations = 0.000171 s +U Equations = 0.001165 s +Y Equations = 0.00209661 s +E Equations = 0.000486 s +p Equations = 0.002128 s +calculate parcels = 39.9707 s +chemistry correctThermo = 0.001946 s +turbulence correct = 0.000964 s +combustion correct(in Y) = 0.0811094 s +percentage of chemistry = 89.8669 % +percentage of rho/U/Y/E = 4.34171 % +========Time details of each equation======= +rhoEqn Time = 0.0003 s +rhoEqn assamble = 0.000238 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001164 s +UEqn assamble = 0.000713 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000451 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001466 s +YEqn assamble = 0.000552 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.4e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000366 s +EEqn assamble = 0.000275 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 71.5 s ClockTime = 72 s +Courant Number mean: 0.00108202 max: 0.0173117 +Time = 0.0008875 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 54 new parcels + +Cloud: sprayCloud + Current number of parcels = 15444 + Current mass in system = 1.32371e-09 + Linear momentum = (2.90608e-11 -1.08415e-08 0) + |Linear momentum| = 1.08415e-08 + Linear kinetic energy = 4.67309e-08 + model1: + number of parcels added = 15460 + mass introduced = 1.36403e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.118, 532.564 + Mass transfer phase change = 4.03171e-11 + D10, D32, Dmax (mu) = 50.7941, 82.965, 150.061 + Liquid penetration 95% mass (m) = 0.00667177 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00630659, Final residual = 9.62954e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.0108955, Final residual = 2.98032e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00184169, Final residual = 1.01648e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00250597, Final residual = 1.37613e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00287779, Final residual = 1.81915e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00287779, Final residual = 1.82071e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00195997, Final residual = 8.74493e-08, No Iterations 1 +min/max(T) = 613.246, 1022.71 +GAMG: Solving for p, Initial residual = 0.0603758, Final residual = 0.000197918, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.02513e-06, global = 2.93584e-06, cumulative = 0.000927441 +GAMG: Solving for p, Initial residual = 0.000187982, Final residual = 4.5974e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.94341e-06, global = 2.94321e-06, cumulative = 0.000930384 +smoothSolver: Solving for epsilon, Initial residual = 0.000906384, Final residual = 1.293e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00213239, Final residual = 3.41654e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.070729 s +other Time = 1e-06 s +rho Equations = 0.000151 s +U Equations = 0.001014 s +Y Equations = 0.00227837 s +E Equations = 0.00048 s +p Equations = 0.001819 s +calculate parcels = 40.1597 s +chemistry correctThermo = 0.001899 s +turbulence correct = 0.000822 s +combustion correct(in Y) = 0.0620916 s +percentage of chemistry = 87.7881 % +percentage of rho/U/Y/E = 5.54704 % +========Time details of each equation======= +rhoEqn Time = 0.000294 s +rhoEqn assamble = 0.00022 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001013 s +UEqn assamble = 0.00064 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000373 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001621 s +YEqn assamble = 0.000584 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000101 s +YEqn correct boundary = 0 s +EEqn Time = 0.000362 s +EEqn assamble = 0.000272 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 71.76 s ClockTime = 72 s +Courant Number mean: 0.00109473 max: 0.0173126 +Time = 0.00089 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 54 new parcels + +Cloud: sprayCloud + Current number of parcels = 15498 + Current mass in system = 1.32628e-09 + Linear momentum = (2.86891e-11 -1.08481e-08 0) + |Linear momentum| = 1.08481e-08 + Linear kinetic energy = 4.66935e-08 + model1: + number of parcels added = 15514 + mass introduced = 1.36685e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.136, 532.638 + Mass transfer phase change = 4.0573e-11 + D10, D32, Dmax (mu) = 50.8034, 82.9979, 150.071 + Liquid penetration 95% mass (m) = 0.00668715 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00655974, Final residual = 2.00803e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0109839, Final residual = 3.01321e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00183268, Final residual = 1.01478e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00250968, Final residual = 1.38338e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00288389, Final residual = 1.827e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00288389, Final residual = 1.82856e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196399, Final residual = 8.76906e-08, No Iterations 1 +min/max(T) = 613.283, 1025.84 +GAMG: Solving for p, Initial residual = 0.0607311, Final residual = 0.000141284, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00946e-06, global = 2.94466e-06, cumulative = 0.000933329 +GAMG: Solving for p, Initial residual = 0.000134053, Final residual = 2.73899e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.94869e-06, global = 2.94857e-06, cumulative = 0.000936278 +smoothSolver: Solving for epsilon, Initial residual = 0.000904801, Final residual = 1.28716e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00212647, Final residual = 3.40987e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.0987 s +other Time = 1e-06 s +rho Equations = 0.000145 s +U Equations = 0.001052 s +Y Equations = 0.00243169 s +E Equations = 0.000634 s +p Equations = 0.00227 s +calculate parcels = 40.4054 s +chemistry correctThermo = 0.002778 s +turbulence correct = 0.001059 s +combustion correct(in Y) = 0.0881563 s +percentage of chemistry = 89.3174 % +percentage of rho/U/Y/E = 4.31883 % +========Time details of each equation======= +rhoEqn Time = 0.000294 s +rhoEqn assamble = 0.000236 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001051 s +UEqn assamble = 0.000579 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000472 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001856 s +YEqn assamble = 0.000697 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000232 s +YEqn correct boundary = 0 s +EEqn Time = 0.000474 s +EEqn assamble = 0.000355 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000119 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 72.1 s ClockTime = 73 s +Courant Number mean: 0.00110787 max: 0.0173049 +Time = 0.0008925 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 45 new parcels + +Cloud: sprayCloud + Current number of parcels = 15542 + Current mass in system = 1.32836e-09 + Linear momentum = (2.83043e-11 -1.08509e-08 0) + |Linear momentum| = 1.08509e-08 + Linear kinetic energy = 4.66409e-08 + model1: + number of parcels added = 15559 + mass introduced = 1.36919e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.14, 532.644 + Mass transfer phase change = 4.08302e-11 + D10, D32, Dmax (mu) = 51.0898, 83.0062, 150.081 + Liquid penetration 95% mass (m) = 0.00670287 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0066796, Final residual = 2.11099e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.01108, Final residual = 3.04572e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00183453, Final residual = 1.03176e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00251512, Final residual = 1.39367e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00288944, Final residual = 1.83591e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00288944, Final residual = 1.83752e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196864, Final residual = 8.84902e-08, No Iterations 1 +min/max(T) = 613.337, 1029.02 +GAMG: Solving for p, Initial residual = 0.06047, Final residual = 0.000145532, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.02525e-06, global = 2.96142e-06, cumulative = 0.000939239 +GAMG: Solving for p, Initial residual = 0.000135882, Final residual = 2.85049e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.96563e-06, global = 2.9655e-06, cumulative = 0.000942205 +smoothSolver: Solving for epsilon, Initial residual = 0.000903262, Final residual = 1.2811e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00212023, Final residual = 3.40221e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.089659 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001239 s +Y Equations = 0.00266079 s +E Equations = 0.00063 s +p Equations = 0.00183 s +calculate parcels = 40.6889 s +chemistry correctThermo = 0.002234 s +turbulence correct = 0.000815 s +combustion correct(in Y) = 0.0798602 s +percentage of chemistry = 89.071 % +percentage of rho/U/Y/E = 5.24966 % +========Time details of each equation======= +rhoEqn Time = 0.000298 s +rhoEqn assamble = 0.000236 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001239 s +UEqn assamble = 0.000725 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000514 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002004 s +YEqn assamble = 0.000719 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000253 s +YEqn correct boundary = 0 s +EEqn Time = 0.000471 s +EEqn assamble = 0.000342 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000129 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 72.47 s ClockTime = 73 s +Courant Number mean: 0.00112134 max: 0.0173022 +Time = 0.000895 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 15586 + Current mass in system = 1.33036e-09 + Linear momentum = (2.82253e-11 -1.0853e-08 0) + |Linear momentum| = 1.08531e-08 + Linear kinetic energy = 4.65857e-08 + model1: + number of parcels added = 15603 + mass introduced = 1.37145e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.119, 532.581 + Mass transfer phase change = 4.1087e-11 + D10, D32, Dmax (mu) = 51.0895, 83.0332, 150.091 + Liquid penetration 95% mass (m) = 0.00671753 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00664305, Final residual = 2.13962e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0111766, Final residual = 3.08001e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00182096, Final residual = 1.01204e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00251776, Final residual = 1.3982e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00289733, Final residual = 1.84587e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00289733, Final residual = 1.84749e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00196972, Final residual = 8.86082e-08, No Iterations 1 +min/max(T) = 613.41, 1032.25 +GAMG: Solving for p, Initial residual = 0.0603118, Final residual = 0.000115297, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.01009e-06, global = 2.9553e-06, cumulative = 0.00094516 +GAMG: Solving for p, Initial residual = 0.000109976, Final residual = 2.04629e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.95967e-06, global = 2.95958e-06, cumulative = 0.000948119 +smoothSolver: Solving for epsilon, Initial residual = 0.000901973, Final residual = 1.27628e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00211455, Final residual = 3.39635e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.091275 s +other Time = 0 s +rho Equations = 0.000273 s +U Equations = 0.001273 s +Y Equations = 0.0024349 s +E Equations = 0.0006 s +p Equations = 0.003255 s +calculate parcels = 40.9333 s +chemistry correctThermo = 0.002763 s +turbulence correct = 0.001756 s +combustion correct(in Y) = 0.0786771 s +percentage of chemistry = 86.1979 % +percentage of rho/U/Y/E = 5.01879 % +========Time details of each equation======= +rhoEqn Time = 0.000495 s +rhoEqn assamble = 0.00034 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000155 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001273 s +UEqn assamble = 0.000765 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000508 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001791 s +YEqn assamble = 0.000688 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000181 s +YEqn correct boundary = 0 s +EEqn Time = 0.000442 s +EEqn assamble = 0.000331 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 72.81 s ClockTime = 73 s +Courant Number mean: 0.00113514 max: 0.0173082 +Time = 0.0008975 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 41 new parcels + +Cloud: sprayCloud + Current number of parcels = 15627 + Current mass in system = 1.33219e-09 + Linear momentum = (2.84374e-11 -1.08537e-08 0) + |Linear momentum| = 1.08538e-08 + Linear kinetic energy = 4.65252e-08 + model1: + number of parcels added = 15644 + mass introduced = 1.37353e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.131, 532.432 + Mass transfer phase change = 4.13443e-11 + D10, D32, Dmax (mu) = 51.052, 83.0413, 150.102 + Liquid penetration 95% mass (m) = 0.00673188 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00664304, Final residual = 2.12506e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0112535, Final residual = 3.10454e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00181954, Final residual = 1.01343e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00252318, Final residual = 1.40368e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00290563, Final residual = 1.85637e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00290563, Final residual = 1.85801e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00197452, Final residual = 8.89356e-08, No Iterations 1 +min/max(T) = 613.505, 1035.54 +GAMG: Solving for p, Initial residual = 0.0602681, Final residual = 9.89479e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.01048e-06, global = 2.96233e-06, cumulative = 0.000951082 +GAMG: Solving for p, Initial residual = 9.2187e-05, Final residual = 9.03439e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.9664e-06, global = 2.96596e-06, cumulative = 0.000954048 +smoothSolver: Solving for epsilon, Initial residual = 0.000900332, Final residual = 1.27157e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00210882, Final residual = 3.38935e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.099271 s +other Time = 1e-06 s +rho Equations = 0.000181 s +U Equations = 0.001228 s +Y Equations = 0.00257605 s +E Equations = 0.000607 s +p Equations = 0.001997 s +calculate parcels = 41.2043 s +chemistry correctThermo = 0.002826 s +turbulence correct = 0.000961 s +combustion correct(in Y) = 0.088688 s +percentage of chemistry = 89.3392 % +percentage of rho/U/Y/E = 4.62577 % +========Time details of each equation======= +rhoEqn Time = 0.000321 s +rhoEqn assamble = 0.000254 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001228 s +UEqn assamble = 0.000722 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000506 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001929 s +YEqn assamble = 0.000656 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000201 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000334 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 73.18 s ClockTime = 74 s +Courant Number mean: 0.00114933 max: 0.0172985 +Time = 0.0009 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 43 new parcels + +Cloud: sprayCloud + Current number of parcels = 15670 + Current mass in system = 1.33409e-09 + Linear momentum = (2.8202e-11 -1.0855e-08 0) + |Linear momentum| = 1.08551e-08 + Linear kinetic energy = 4.64669e-08 + model1: + number of parcels added = 15687 + mass introduced = 1.37569e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.118, 532.194 + Mass transfer phase change = 4.16021e-11 + D10, D32, Dmax (mu) = 51.0384, 83.0631, 150.112 + Liquid penetration 95% mass (m) = 0.00674689 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00664574, Final residual = 2.13744e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0113393, Final residual = 3.1353e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00182143, Final residual = 1.0203e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00252841, Final residual = 1.40933e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00291385, Final residual = 1.86715e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00291384, Final residual = 1.86879e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00198009, Final residual = 8.94056e-08, No Iterations 1 +min/max(T) = 613.611, 1038.89 +GAMG: Solving for p, Initial residual = 0.0602015, Final residual = 9.34776e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.01231e-06, global = 2.96765e-06, cumulative = 0.000957015 +GAMG: Solving for p, Initial residual = 8.71637e-05, Final residual = 8.74714e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.97143e-06, global = 2.971e-06, cumulative = 0.000959986 +smoothSolver: Solving for epsilon, Initial residual = 0.000899379, Final residual = 1.26703e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00210298, Final residual = 3.38224e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097435 s +other Time = 0 s +rho Equations = 0.000225 s +U Equations = 0.001195 s +Y Equations = 0.00245483 s +E Equations = 0.000605 s +p Equations = 0.00197 s +calculate parcels = 41.4695 s +chemistry correctThermo = 0.00279 s +turbulence correct = 0.001 s +combustion correct(in Y) = 0.0870132 s +percentage of chemistry = 89.3038 % +percentage of rho/U/Y/E = 4.59777 % +========Time details of each equation======= +rhoEqn Time = 0.000362 s +rhoEqn assamble = 0.000293 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001195 s +UEqn assamble = 0.000689 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000506 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001794 s +YEqn assamble = 0.000651 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000175 s +YEqn correct boundary = 0 s +EEqn Time = 0.000449 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 73.79 s ClockTime = 74 s +Courant Number mean: 0.00116386 max: 0.01729 +Time = 0.0009025 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 43 new parcels + +Cloud: sprayCloud + Current number of parcels = 15713 + Current mass in system = 1.33596e-09 + Linear momentum = (2.83932e-11 -1.08561e-08 0) + |Linear momentum| = 1.08561e-08 + Linear kinetic energy = 4.64079e-08 + model1: + number of parcels added = 15730 + mass introduced = 1.37782e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.119, 531.868 + Mass transfer phase change = 4.18603e-11 + D10, D32, Dmax (mu) = 51.0368, 83.0881, 150.122 + Liquid penetration 95% mass (m) = 0.00676297 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00672183, Final residual = 2.16919e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0114302, Final residual = 3.1725e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00181973, Final residual = 1.02114e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00253405, Final residual = 1.42281e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00292261, Final residual = 1.87776e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00292261, Final residual = 1.87942e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00198466, Final residual = 8.96557e-08, No Iterations 1 +min/max(T) = 613.732, 1042.31 +GAMG: Solving for p, Initial residual = 0.0601422, Final residual = 8.98581e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.01452e-06, global = 2.97209e-06, cumulative = 0.000962958 +GAMG: Solving for p, Initial residual = 8.40827e-05, Final residual = 5.95799e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.97588e-06, global = 2.97559e-06, cumulative = 0.000965934 +smoothSolver: Solving for epsilon, Initial residual = 0.000899072, Final residual = 1.26286e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00209687, Final residual = 3.37464e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.068763 s +other Time = 1e-06 s +rho Equations = 0.000178 s +U Equations = 0.001208 s +Y Equations = 0.00223987 s +E Equations = 0.000512 s +p Equations = 0.001962 s +calculate parcels = 41.6788 s +chemistry correctThermo = 0.001925 s +turbulence correct = 0.00085 s +combustion correct(in Y) = 0.0597101 s +percentage of chemistry = 86.8347 % +percentage of rho/U/Y/E = 6.01759 % +========Time details of each equation======= +rhoEqn Time = 0.000309 s +rhoEqn assamble = 0.000244 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001207 s +UEqn assamble = 0.000678 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000529 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001656 s +YEqn assamble = 0.000585 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00013 s +YEqn correct boundary = 0 s +EEqn Time = 0.000386 s +EEqn assamble = 0.000291 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 74.07 s ClockTime = 75 s +Courant Number mean: 0.00117868 max: 0.0172854 +Time = 0.000905 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 60 new parcels + +Cloud: sprayCloud + Current number of parcels = 15773 + Current mass in system = 1.33865e-09 + Linear momentum = (2.78675e-11 -1.08631e-08 0) + |Linear momentum| = 1.08632e-08 + Linear kinetic energy = 4.63718e-08 + model1: + number of parcels added = 15790 + mass introduced = 1.38077e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.111, 531.453 + Mass transfer phase change = 4.21189e-11 + D10, D32, Dmax (mu) = 51.0267, 83.1049, 150.132 + Liquid penetration 95% mass (m) = 0.00677893 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00683312, Final residual = 2.2107e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0115336, Final residual = 3.21841e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00181899, Final residual = 1.0262e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00253996, Final residual = 1.43434e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00293142, Final residual = 1.88823e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00293142, Final residual = 1.8899e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00198905, Final residual = 8.98255e-08, No Iterations 1 +min/max(T) = 613.874, 1045.78 +GAMG: Solving for p, Initial residual = 0.0599708, Final residual = 8.16354e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.01721e-06, global = 2.97747e-06, cumulative = 0.000968911 +GAMG: Solving for p, Initial residual = 7.67828e-05, Final residual = 8.92632e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.98104e-06, global = 2.98064e-06, cumulative = 0.000971892 +smoothSolver: Solving for epsilon, Initial residual = 0.000898913, Final residual = 1.25888e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00209097, Final residual = 3.36771e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097475 s +other Time = 1e-06 s +rho Equations = 0.00017 s +U Equations = 0.00119 s +Y Equations = 0.0024759 s +E Equations = 0.000607 s +p Equations = 0.002031 s +calculate parcels = 41.9016 s +chemistry correctThermo = 0.002828 s +turbulence correct = 0.000966 s +combustion correct(in Y) = 0.0870111 s +percentage of chemistry = 89.265 % +percentage of rho/U/Y/E = 4.55799 % +========Time details of each equation======= +rhoEqn Time = 0.000309 s +rhoEqn assamble = 0.00024 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00119 s +UEqn assamble = 0.000658 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000532 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001831 s +YEqn assamble = 0.000711 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000193 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 74.39 s ClockTime = 75 s +Courant Number mean: 0.00119388 max: 0.0172775 +Time = 0.0009075 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 54 new parcels + +Cloud: sprayCloud + Current number of parcels = 15827 + Current mass in system = 1.34103e-09 + Linear momentum = (2.7777e-11 -1.08679e-08 0) + |Linear momentum| = 1.08679e-08 + Linear kinetic energy = 4.63267e-08 + model1: + number of parcels added = 15844 + mass introduced = 1.38341e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.112, 530.947 + Mass transfer phase change = 4.23778e-11 + D10, D32, Dmax (mu) = 51.0373, 83.1436, 150.143 + Liquid penetration 95% mass (m) = 0.00679477 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00677067, Final residual = 2.20662e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0116389, Final residual = 3.25911e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0018113, Final residual = 1.03673e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.002546, Final residual = 1.44638e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00294072, Final residual = 1.89915e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00294072, Final residual = 1.90083e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00199285, Final residual = 9.03435e-08, No Iterations 1 +min/max(T) = 614.041, 1049.31 +GAMG: Solving for p, Initial residual = 0.0598177, Final residual = 7.41822e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.01836e-06, global = 2.98116e-06, cumulative = 0.000974873 +GAMG: Solving for p, Initial residual = 6.94671e-05, Final residual = 5.62891e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.98469e-06, global = 2.98441e-06, cumulative = 0.000977858 +smoothSolver: Solving for epsilon, Initial residual = 0.00089819, Final residual = 1.25444e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00208526, Final residual = 3.36072e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.087742 s +other Time = 0 s +rho Equations = 0.00019 s +U Equations = 0.001217 s +Y Equations = 0.00204556 s +E Equations = 0.000485 s +p Equations = 0.001675 s +calculate parcels = 42.1702 s +chemistry correctThermo = 0.002823 s +turbulence correct = 0.000826 s +combustion correct(in Y) = 0.0783054 s +percentage of chemistry = 89.2451 % +percentage of rho/U/Y/E = 4.48766 % +========Time details of each equation======= +rhoEqn Time = 0.000309 s +rhoEqn assamble = 0.000241 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001216 s +UEqn assamble = 0.000722 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000494 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001345 s +YEqn assamble = 0.000519 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 5.5e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000367 s +EEqn assamble = 0.000275 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 74.75 s ClockTime = 75 s +Courant Number mean: 0.00120945 max: 0.0172712 +Time = 0.00091 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 70 new parcels + +Cloud: sprayCloud + Current number of parcels = 15897 + Current mass in system = 1.34417e-09 + Linear momentum = (2.74992e-11 -1.08782e-08 0) + |Linear momentum| = 1.08782e-08 + Linear kinetic energy = 4.63023e-08 + model1: + number of parcels added = 15914 + mass introduced = 1.38681e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.109, 530.346 + Mass transfer phase change = 4.26371e-11 + D10, D32, Dmax (mu) = 51.0392, 83.1772, 150.153 + Liquid penetration 95% mass (m) = 0.00681098 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00681055, Final residual = 2.20818e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0117234, Final residual = 3.29287e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00180565, Final residual = 1.03851e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00255219, Final residual = 1.45601e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00295, Final residual = 1.91029e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00294999, Final residual = 1.91198e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00199745, Final residual = 9.05474e-08, No Iterations 1 +min/max(T) = 614.231, 1052.91 +GAMG: Solving for p, Initial residual = 0.0596849, Final residual = 7.00172e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.02179e-06, global = 2.98559e-06, cumulative = 0.000980843 +GAMG: Solving for p, Initial residual = 6.61173e-05, Final residual = 5.70404e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.98868e-06, global = 2.98838e-06, cumulative = 0.000983832 +smoothSolver: Solving for epsilon, Initial residual = 0.000897322, Final residual = 1.25014e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00207935, Final residual = 3.35318e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103467 s +other Time = 1e-06 s +rho Equations = 0.000145 s +U Equations = 0.000989 s +Y Equations = 0.00235836 s +E Equations = 0.000597 s +p Equations = 0.002077 s +calculate parcels = 42.4333 s +chemistry correctThermo = 0.002815 s +turbulence correct = 0.001093 s +combustion correct(in Y) = 0.0932186 s +percentage of chemistry = 90.095 % +percentage of rho/U/Y/E = 3.95233 % +========Time details of each equation======= +rhoEqn Time = 0.000293 s +rhoEqn assamble = 0.000231 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000988 s +UEqn assamble = 0.000576 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000412 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.0018 s +YEqn assamble = 0.000666 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000224 s +YEqn correct boundary = 0 s +EEqn Time = 0.000439 s +EEqn assamble = 0.000328 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 75.12 s ClockTime = 76 s +Courant Number mean: 0.00122546 max: 0.0172624 +Time = 0.0009125 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 42 new parcels + +Cloud: sprayCloud + Current number of parcels = 15939 + Current mass in system = 1.34595e-09 + Linear momentum = (2.76526e-11 -1.08784e-08 0) + |Linear momentum| = 1.08785e-08 + Linear kinetic energy = 4.62407e-08 + model1: + number of parcels added = 15956 + mass introduced = 1.38885e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.109, 529.684 + Mass transfer phase change = 4.28966e-11 + D10, D32, Dmax (mu) = 51.0434, 83.2023, 150.164 + Liquid penetration 95% mass (m) = 0.0068268 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00682913, Final residual = 2.25165e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0118194, Final residual = 3.32845e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00179895, Final residual = 1.04598e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00255869, Final residual = 1.4691e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00296005, Final residual = 1.92192e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00296004, Final residual = 1.92363e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00199927, Final residual = 9.11206e-08, No Iterations 1 +min/max(T) = 614.425, 1056.56 +GAMG: Solving for p, Initial residual = 0.0594972, Final residual = 7.48088e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.02495e-06, global = 2.9881e-06, cumulative = 0.00098682 +GAMG: Solving for p, Initial residual = 7.01525e-05, Final residual = 6.3837e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.99132e-06, global = 2.99098e-06, cumulative = 0.000989811 +smoothSolver: Solving for epsilon, Initial residual = 0.00089664, Final residual = 1.24628e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00207355, Final residual = 3.34661e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09684 s +other Time = 0 s +rho Equations = 0.000181 s +U Equations = 0.00118 s +Y Equations = 0.00245229 s +E Equations = 0.000634 s +p Equations = 0.002117 s +calculate parcels = 42.7057 s +chemistry correctThermo = 0.002819 s +turbulence correct = 0.001053 s +combustion correct(in Y) = 0.0862007 s +percentage of chemistry = 89.0135 % +percentage of rho/U/Y/E = 4.59242 % +========Time details of each equation======= +rhoEqn Time = 0.000345 s +rhoEqn assamble = 0.000263 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001178 s +UEqn assamble = 0.000663 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000515 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001702 s +YEqn assamble = 0.000646 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000148 s +YEqn correct boundary = 0 s +EEqn Time = 0.000475 s +EEqn assamble = 0.000357 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 75.49 s ClockTime = 76 s +Courant Number mean: 0.00124187 max: 0.0172513 +Time = 0.000915 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 43 new parcels + +Cloud: sprayCloud + Current number of parcels = 15982 + Current mass in system = 1.34775e-09 + Linear momentum = (2.73859e-11 -1.08788e-08 0) + |Linear momentum| = 1.08789e-08 + Linear kinetic energy = 4.61797e-08 + model1: + number of parcels added = 15999 + mass introduced = 1.39091e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.133, 529.923 + Mass transfer phase change = 4.31563e-11 + D10, D32, Dmax (mu) = 50.9926, 83.2201, 150.175 + Liquid penetration 95% mass (m) = 0.00684338 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00695728, Final residual = 2.28967e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0119018, Final residual = 3.36313e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00179371, Final residual = 1.05057e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00256538, Final residual = 1.48159e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00297007, Final residual = 1.93427e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00297006, Final residual = 1.93601e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00200338, Final residual = 9.14965e-08, No Iterations 1 +min/max(T) = 614.626, 1060.29 +GAMG: Solving for p, Initial residual = 0.0592891, Final residual = 6.50899e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.02732e-06, global = 2.9912e-06, cumulative = 0.000992802 +GAMG: Solving for p, Initial residual = 6.05728e-05, Final residual = 5.27872e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.99424e-06, global = 2.99394e-06, cumulative = 0.000995796 +smoothSolver: Solving for epsilon, Initial residual = 0.000896169, Final residual = 1.24495e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00206802, Final residual = 3.34045e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.101573 s +other Time = 0 s +rho Equations = 0.000165 s +U Equations = 0.001256 s +Y Equations = 0.00239276 s +E Equations = 0.000608 s +p Equations = 0.002008 s +calculate parcels = 42.9742 s +chemistry correctThermo = 0.002804 s +turbulence correct = 0.00101 s +combustion correct(in Y) = 0.0910702 s +percentage of chemistry = 89.6599 % +percentage of rho/U/Y/E = 4.35329 % +========Time details of each equation======= +rhoEqn Time = 0.000306 s +rhoEqn assamble = 0.000241 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001255 s +UEqn assamble = 0.000706 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000549 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001735 s +YEqn assamble = 0.000645 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000169 s +YEqn correct boundary = 0 s +EEqn Time = 0.000455 s +EEqn assamble = 0.000338 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 75.86 s ClockTime = 76 s +Courant Number mean: 0.00125869 max: 0.0172374 +Time = 0.0009175 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 45 new parcels + +Cloud: sprayCloud + Current number of parcels = 16026 + Current mass in system = 1.34963e-09 + Linear momentum = (2.73307e-11 -1.08797e-08 0) + |Linear momentum| = 1.08797e-08 + Linear kinetic energy = 4.61208e-08 + model1: + number of parcels added = 16044 + mass introduced = 1.39305e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.127, 531.895 + Mass transfer phase change = 4.34172e-11 + D10, D32, Dmax (mu) = 51.5718, 83.2459, 150.185 + Liquid penetration 95% mass (m) = 0.0068587 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00703027, Final residual = 2.33195e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0119942, Final residual = 3.3985e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00179956, Final residual = 1.0726e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0025744, Final residual = 1.49811e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00298083, Final residual = 1.94656e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00298083, Final residual = 1.94831e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00201219, Final residual = 9.24806e-08, No Iterations 1 +min/max(T) = 614.848, 1064.07 +GAMG: Solving for p, Initial residual = 0.0590948, Final residual = 6.87378e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.04034e-06, global = 3.00397e-06, cumulative = 0.0009988 +GAMG: Solving for p, Initial residual = 6.44784e-05, Final residual = 5.60577e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00707e-06, global = 3.00677e-06, cumulative = 0.00100181 +smoothSolver: Solving for epsilon, Initial residual = 0.000895554, Final residual = 1.2445e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00206296, Final residual = 3.33463e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.098813 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001197 s +Y Equations = 0.002449 s +E Equations = 0.000605 s +p Equations = 0.002044 s +calculate parcels = 43.2521 s +chemistry correctThermo = 0.002782 s +turbulence correct = 0.001054 s +combustion correct(in Y) = 0.088271 s +percentage of chemistry = 89.3314 % +percentage of rho/U/Y/E = 4.48119 % +========Time details of each equation======= +rhoEqn Time = 0.000319 s +rhoEqn assamble = 0.000252 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001196 s +UEqn assamble = 0.000668 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000528 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001793 s +YEqn assamble = 0.000645 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000188 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 76.23 s ClockTime = 77 s +Courant Number mean: 0.00127599 max: 0.0172279 +Time = 0.00092 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 16074 + Current mass in system = 1.35164e-09 + Linear momentum = (2.73307e-11 -1.08817e-08 0) + |Linear momentum| = 1.08817e-08 + Linear kinetic energy = 4.60665e-08 + model1: + number of parcels added = 16092 + mass introduced = 1.39532e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.118, 533.555 + Mass transfer phase change = 4.36771e-11 + D10, D32, Dmax (mu) = 51.5723, 83.265, 150.192 + Liquid penetration 95% mass (m) = 0.00687413 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00706015, Final residual = 2.34492e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0120859, Final residual = 3.43354e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00178915, Final residual = 1.06675e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00257914, Final residual = 1.50692e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00299157, Final residual = 1.96035e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00299156, Final residual = 1.96209e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00201556, Final residual = 9.25888e-08, No Iterations 1 +min/max(T) = 615.09, 1067.92 +GAMG: Solving for p, Initial residual = 0.0588518, Final residual = 7.04797e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.03244e-06, global = 2.99238e-06, cumulative = 0.0010048 +GAMG: Solving for p, Initial residual = 6.56688e-05, Final residual = 7.01964e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.99578e-06, global = 2.99536e-06, cumulative = 0.00100779 +smoothSolver: Solving for epsilon, Initial residual = 0.000894766, Final residual = 1.24454e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00205789, Final residual = 3.3284e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.069615 s +other Time = 0 s +rho Equations = 0.000174 s +U Equations = 0.001108 s +Y Equations = 0.00215622 s +E Equations = 0.000487 s +p Equations = 0.001717 s +calculate parcels = 43.4551 s +chemistry correctThermo = 0.001986 s +turbulence correct = 0.000976 s +combustion correct(in Y) = 0.0608088 s +percentage of chemistry = 87.3501 % +percentage of rho/U/Y/E = 5.63847 % +========Time details of each equation======= +rhoEqn Time = 0.000295 s +rhoEqn assamble = 0.00024 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001107 s +UEqn assamble = 0.000666 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000441 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001495 s +YEqn assamble = 0.000565 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.2e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000367 s +EEqn assamble = 0.000276 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 76.51 s ClockTime = 77 s +Courant Number mean: 0.00129375 max: 0.0172163 +Time = 0.0009225 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 66 new parcels + +Cloud: sprayCloud + Current number of parcels = 16140 + Current mass in system = 1.35451e-09 + Linear momentum = (2.74294e-11 -1.089e-08 0) + |Linear momentum| = 1.08901e-08 + Linear kinetic energy = 4.60361e-08 + model1: + number of parcels added = 16158 + mass introduced = 1.39845e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.111, 534.934 + Mass transfer phase change = 4.39371e-11 + D10, D32, Dmax (mu) = 51.5616, 83.2977, 150.18 + Liquid penetration 95% mass (m) = 0.00688916 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00722588, Final residual = 2.38801e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.012175, Final residual = 3.47159e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00178668, Final residual = 1.07651e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00258706, Final residual = 1.51872e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00300324, Final residual = 1.97615e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00300324, Final residual = 1.97795e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00202407, Final residual = 9.29718e-08, No Iterations 1 +min/max(T) = 615.334, 1071.84 +GAMG: Solving for p, Initial residual = 0.0585953, Final residual = 7.16293e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.03442e-06, global = 2.99446e-06, cumulative = 0.00101079 +GAMG: Solving for p, Initial residual = 6.59514e-05, Final residual = 6.50529e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.99755e-06, global = 2.99718e-06, cumulative = 0.00101379 +smoothSolver: Solving for epsilon, Initial residual = 0.000894381, Final residual = 1.24557e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00205409, Final residual = 3.3237e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.087773 s +other Time = 0 s +rho Equations = 0.000144 s +U Equations = 0.001001 s +Y Equations = 0.00236709 s +E Equations = 0.000597 s +p Equations = 0.002073 s +calculate parcels = 43.6917 s +chemistry correctThermo = 0.002748 s +turbulence correct = 0.001065 s +combustion correct(in Y) = 0.0775989 s +percentage of chemistry = 88.4086 % +percentage of rho/U/Y/E = 4.68149 % +========Time details of each equation======= +rhoEqn Time = 0.000288 s +rhoEqn assamble = 0.000229 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000999 s +UEqn assamble = 0.000579 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00042 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00181 s +YEqn assamble = 0.000642 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000239 s +YEqn correct boundary = 0 s +EEqn Time = 0.000444 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 76.83 s ClockTime = 77 s +Courant Number mean: 0.00131205 max: 0.0172116 +Time = 0.000925 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 16186 + Current mass in system = 1.35645e-09 + Linear momentum = (2.7e-11 -1.08918e-08 0) + |Linear momentum| = 1.08919e-08 + Linear kinetic energy = 4.59825e-08 + model1: + number of parcels added = 16204 + mass introduced = 1.40065e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.122, 536.062 + Mass transfer phase change = 4.41973e-11 + D10, D32, Dmax (mu) = 51.5573, 83.319, 150.177 + Liquid penetration 95% mass (m) = 0.00690489 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00734395, Final residual = 2.45178e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0122665, Final residual = 3.50989e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00178556, Final residual = 1.08675e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00259498, Final residual = 1.52944e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00301495, Final residual = 1.99238e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00301494, Final residual = 1.99421e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00203284, Final residual = 9.32548e-08, No Iterations 1 +min/max(T) = 615.59, 1075.83 +GAMG: Solving for p, Initial residual = 0.0583376, Final residual = 5.63972e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.02838e-06, global = 2.99611e-06, cumulative = 0.00101678 +GAMG: Solving for p, Initial residual = 5.24466e-05, Final residual = 4.69565e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.99876e-06, global = 2.99853e-06, cumulative = 0.00101978 +smoothSolver: Solving for epsilon, Initial residual = 0.000893894, Final residual = 1.24711e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00205018, Final residual = 3.31927e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094336 s +other Time = 0 s +rho Equations = 0.00017 s +U Equations = 0.001173 s +Y Equations = 0.00242457 s +E Equations = 0.0006 s +p Equations = 0.002009 s +calculate parcels = 43.9595 s +chemistry correctThermo = 0.002784 s +turbulence correct = 0.001088 s +combustion correct(in Y) = 0.0838864 s +percentage of chemistry = 88.923 % +percentage of rho/U/Y/E = 4.6298 % +========Time details of each equation======= +rhoEqn Time = 0.000308 s +rhoEqn assamble = 0.000247 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001173 s +UEqn assamble = 0.000678 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000495 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001785 s +YEqn assamble = 0.000663 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000193 s +YEqn correct boundary = 0 s +EEqn Time = 0.000444 s +EEqn assamble = 0.00033 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 77.19 s ClockTime = 78 s +Courant Number mean: 0.00133086 max: 0.0172204 +Time = 0.0009275 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 40 new parcels + +Cloud: sprayCloud + Current number of parcels = 16226 + Current mass in system = 1.35811e-09 + Linear momentum = (2.72463e-11 -1.08917e-08 0) + |Linear momentum| = 1.08917e-08 + Linear kinetic energy = 4.59228e-08 + model1: + number of parcels added = 16244 + mass introduced = 1.40257e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.127, 536.97 + Mass transfer phase change = 4.44575e-11 + D10, D32, Dmax (mu) = 51.5615, 83.3519, 150.186 + Liquid penetration 95% mass (m) = 0.00691961 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0074868, Final residual = 2.52231e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0123499, Final residual = 3.54483e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00178558, Final residual = 1.09921e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0026036, Final residual = 1.53958e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00302772, Final residual = 2.00985e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00302771, Final residual = 2.01167e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00204108, Final residual = 9.37033e-08, No Iterations 1 +min/max(T) = 615.868, 1079.88 +GAMG: Solving for p, Initial residual = 0.0580975, Final residual = 6.48644e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.0349e-06, global = 2.99672e-06, cumulative = 0.00102278 +GAMG: Solving for p, Initial residual = 6.10208e-05, Final residual = 5.5073e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.99963e-06, global = 2.99931e-06, cumulative = 0.00102578 +smoothSolver: Solving for epsilon, Initial residual = 0.000893276, Final residual = 1.24985e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0020463, Final residual = 3.31465e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102723 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001197 s +Y Equations = 0.00239044 s +E Equations = 0.000665 s +p Equations = 0.00203 s +calculate parcels = 44.2361 s +chemistry correctThermo = 0.002789 s +turbulence correct = 0.000965 s +combustion correct(in Y) = 0.0923126 s +percentage of chemistry = 89.8655 % +percentage of rho/U/Y/E = 4.31202 % +========Time details of each equation======= +rhoEqn Time = 0.00032 s +rhoEqn assamble = 0.000255 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001196 s +UEqn assamble = 0.000669 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000527 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001722 s +YEqn assamble = 0.000643 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000158 s +YEqn correct boundary = 0 s +EEqn Time = 0.000482 s +EEqn assamble = 0.000363 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000119 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 77.57 s ClockTime = 78 s +Courant Number mean: 0.00135021 max: 0.0172244 +Time = 0.00093 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 16277 + Current mass in system = 1.36029e-09 + Linear momentum = (2.72129e-11 -1.08955e-08 0) + |Linear momentum| = 1.08955e-08 + Linear kinetic energy = 4.58782e-08 + model1: + number of parcels added = 16295 + mass introduced = 1.40501e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.117, 537.688 + Mass transfer phase change = 4.47178e-11 + D10, D32, Dmax (mu) = 51.5433, 83.3738, 150.195 + Liquid penetration 95% mass (m) = 0.0069343 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00770879, Final residual = 2.59033e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0124223, Final residual = 3.57771e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00177908, Final residual = 1.10792e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00261271, Final residual = 1.55229e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00304103, Final residual = 2.02808e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00304102, Final residual = 2.02994e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00204881, Final residual = 9.46282e-08, No Iterations 1 +min/max(T) = 616.157, 1084 +GAMG: Solving for p, Initial residual = 0.0578197, Final residual = 6.15951e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.03454e-06, global = 2.99797e-06, cumulative = 0.00102877 +GAMG: Solving for p, Initial residual = 5.70048e-05, Final residual = 5.5194e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00071e-06, global = 3.00038e-06, cumulative = 0.00103178 +smoothSolver: Solving for epsilon, Initial residual = 0.000893983, Final residual = 1.25203e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00204313, Final residual = 3.31174e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.071127 s +other Time = 1e-06 s +rho Equations = 0.000148 s +U Equations = 0.001023 s +Y Equations = 0.00204984 s +E Equations = 0.000559 s +p Equations = 0.001712 s +calculate parcels = 44.4534 s +chemistry correctThermo = 0.001984 s +turbulence correct = 0.000885 s +combustion correct(in Y) = 0.0625972 s +percentage of chemistry = 88.0076 % +percentage of rho/U/Y/E = 5.31421 % +========Time details of each equation======= +rhoEqn Time = 0.000268 s +rhoEqn assamble = 0.000211 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001021 s +UEqn assamble = 0.000594 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000427 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001478 s +YEqn assamble = 0.000533 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000127 s +YEqn correct boundary = 0 s +EEqn Time = 0.000398 s +EEqn assamble = 0.000297 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000101 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 77.86 s ClockTime = 78 s +Courant Number mean: 0.00137006 max: 0.0172218 +Time = 0.0009325 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 16325 + Current mass in system = 1.36233e-09 + Linear momentum = (2.68417e-11 -1.08985e-08 0) + |Linear momentum| = 1.08985e-08 + Linear kinetic energy = 4.58311e-08 + model1: + number of parcels added = 16343 + mass introduced = 1.40731e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.138, 538.247 + Mass transfer phase change = 4.49783e-11 + D10, D32, Dmax (mu) = 51.461, 83.3806, 150.204 + Liquid penetration 95% mass (m) = 0.00694924 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0079106, Final residual = 2.68082e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0125035, Final residual = 3.61362e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00177705, Final residual = 1.09668e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00262211, Final residual = 1.56456e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00305447, Final residual = 2.04746e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00305447, Final residual = 2.04934e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00205731, Final residual = 9.44107e-08, No Iterations 1 +min/max(T) = 616.468, 1088.18 +GAMG: Solving for p, Initial residual = 0.0575375, Final residual = 6.55704e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.04057e-06, global = 2.99898e-06, cumulative = 0.00103477 +GAMG: Solving for p, Initial residual = 6.00183e-05, Final residual = 5.31831e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00232e-06, global = 3.00198e-06, cumulative = 0.00103778 +smoothSolver: Solving for epsilon, Initial residual = 0.000895216, Final residual = 1.25398e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00204001, Final residual = 3.3097e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.070511 s +other Time = 0 s +rho Equations = 0.000171 s +U Equations = 0.001203 s +Y Equations = 0.00213952 s +E Equations = 0.000497 s +p Equations = 0.002039 s +calculate parcels = 44.7093 s +chemistry correctThermo = 0.00233 s +turbulence correct = 0.00084 s +combustion correct(in Y) = 0.0610925 s +percentage of chemistry = 86.6425 % +percentage of rho/U/Y/E = 5.68779 % +========Time details of each equation======= +rhoEqn Time = 0.00031 s +rhoEqn assamble = 0.000245 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001201 s +UEqn assamble = 0.000694 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000507 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001494 s +YEqn assamble = 0.000545 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000118 s +YEqn correct boundary = 0 s +EEqn Time = 0.000377 s +EEqn assamble = 0.000281 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 78.19 s ClockTime = 79 s +Courant Number mean: 0.00139047 max: 0.0172314 +Time = 0.000935 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 54 new parcels + +Cloud: sprayCloud + Current number of parcels = 16379 + Current mass in system = 1.36467e-09 + Linear momentum = (2.69924e-11 -1.09037e-08 0) + |Linear momentum| = 1.09037e-08 + Linear kinetic energy = 4.57932e-08 + model1: + number of parcels added = 16397 + mass introduced = 1.40991e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.12, 538.679 + Mass transfer phase change = 4.52388e-11 + D10, D32, Dmax (mu) = 51.2936, 83.401, 150.213 + Liquid penetration 95% mass (m) = 0.00696422 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00797586, Final residual = 2.71729e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0126013, Final residual = 3.6525e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00177595, Final residual = 1.09354e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00263185, Final residual = 1.57745e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00306831, Final residual = 2.0686e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0030683, Final residual = 2.0705e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00206395, Final residual = 9.46809e-08, No Iterations 1 +min/max(T) = 616.804, 1092.43 +GAMG: Solving for p, Initial residual = 0.0572016, Final residual = 4.91131e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.03506e-06, global = 3.00053e-06, cumulative = 0.00104078 +GAMG: Solving for p, Initial residual = 4.50323e-05, Final residual = 3.22662e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00354e-06, global = 3.00332e-06, cumulative = 0.00104378 +smoothSolver: Solving for epsilon, Initial residual = 0.000896517, Final residual = 1.25612e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00203685, Final residual = 3.30836e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.076714 s +other Time = 1e-06 s +rho Equations = 0.000198 s +U Equations = 0.001307 s +Y Equations = 0.00205221 s +E Equations = 0.000492 s +p Equations = 0.001721 s +calculate parcels = 44.9887 s +chemistry correctThermo = 0.002014 s +turbulence correct = 0.000795 s +combustion correct(in Y) = 0.0679288 s +percentage of chemistry = 88.5481 % +percentage of rho/U/Y/E = 5.27832 % +========Time details of each equation======= +rhoEqn Time = 0.000318 s +rhoEqn assamble = 0.000252 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001307 s +UEqn assamble = 0.000735 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000572 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001356 s +YEqn assamble = 0.000512 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 5.9e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000373 s +EEqn assamble = 0.000278 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 78.54 s ClockTime = 79 s +Courant Number mean: 0.00141138 max: 0.017236 +Time = 0.0009375 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 16425 + Current mass in system = 1.36663e-09 + Linear momentum = (2.69905e-11 -1.09064e-08 0) + |Linear momentum| = 1.09064e-08 + Linear kinetic energy = 4.57465e-08 + model1: + number of parcels added = 16443 + mass introduced = 1.41213e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.124, 539.008 + Mass transfer phase change = 4.54994e-11 + D10, D32, Dmax (mu) = 51.2631, 83.4246, 150.222 + Liquid penetration 95% mass (m) = 0.00698032 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00806871, Final residual = 2.77426e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0126911, Final residual = 3.69222e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00176974, Final residual = 1.09633e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00264155, Final residual = 1.59405e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00308216, Final residual = 2.09002e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00308216, Final residual = 2.09194e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00207129, Final residual = 9.51386e-08, No Iterations 1 +min/max(T) = 617.152, 1096.74 +GAMG: Solving for p, Initial residual = 0.0568811, Final residual = 5.92175e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.03891e-06, global = 3.00055e-06, cumulative = 0.00104678 +GAMG: Solving for p, Initial residual = 5.53262e-05, Final residual = 5.53094e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00385e-06, global = 3.00347e-06, cumulative = 0.00104978 +smoothSolver: Solving for epsilon, Initial residual = 0.000897339, Final residual = 1.25767e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00203379, Final residual = 3.30675e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.068728 s +other Time = 1e-06 s +rho Equations = 0.000158 s +U Equations = 0.001031 s +Y Equations = 0.00208614 s +E Equations = 0.000507 s +p Equations = 0.001818 s +calculate parcels = 45.2055 s +chemistry correctThermo = 0.002 s +turbulence correct = 0.000871 s +combustion correct(in Y) = 0.0600669 s +percentage of chemistry = 87.398 % +percentage of rho/U/Y/E = 5.50305 % +========Time details of each equation======= +rhoEqn Time = 0.000282 s +rhoEqn assamble = 0.000227 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00103 s +UEqn assamble = 0.000619 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000411 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001511 s +YEqn assamble = 0.000534 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000127 s +YEqn correct boundary = 0 s +EEqn Time = 0.000383 s +EEqn assamble = 0.000289 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 78.83 s ClockTime = 79 s +Courant Number mean: 0.00143276 max: 0.0172452 +Time = 0.00094 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 16474 + Current mass in system = 1.36874e-09 + Linear momentum = (2.65305e-11 -1.09102e-08 0) + |Linear momentum| = 1.09103e-08 + Linear kinetic energy = 4.57051e-08 + model1: + number of parcels added = 16492 + mass introduced = 1.4145e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.138, 539.255 + Mass transfer phase change = 4.576e-11 + D10, D32, Dmax (mu) = 51.2693, 83.4468, 150.231 + Liquid penetration 95% mass (m) = 0.00699556 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00820627, Final residual = 2.82126e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0127637, Final residual = 3.72492e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00177132, Final residual = 1.10854e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00265169, Final residual = 1.61346e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00309652, Final residual = 2.11172e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00309651, Final residual = 2.11367e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00207916, Final residual = 9.64649e-08, No Iterations 1 +min/max(T) = 617.51, 1101.12 +GAMG: Solving for p, Initial residual = 0.0565501, Final residual = 5.39428e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.03838e-06, global = 3.00017e-06, cumulative = 0.00105278 +GAMG: Solving for p, Initial residual = 4.99537e-05, Final residual = 4.53415e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00351e-06, global = 3.00319e-06, cumulative = 0.00105579 +smoothSolver: Solving for epsilon, Initial residual = 0.000897954, Final residual = 1.25916e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00203061, Final residual = 3.30588e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.083548 s +other Time = 1e-06 s +rho Equations = 0.000208 s +U Equations = 0.001384 s +Y Equations = 0.00202103 s +E Equations = 0.000473 s +p Equations = 0.001623 s +calculate parcels = 45.4081 s +chemistry correctThermo = 0.002016 s +turbulence correct = 0.000786 s +combustion correct(in Y) = 0.074823 s +percentage of chemistry = 89.5569 % +percentage of rho/U/Y/E = 4.89064 % +========Time details of each equation======= +rhoEqn Time = 0.000324 s +rhoEqn assamble = 0.000257 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001381 s +UEqn assamble = 0.000787 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000594 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001318 s +YEqn assamble = 0.000506 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 5.6e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000359 s +EEqn assamble = 0.000268 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 79.12 s ClockTime = 80 s +Courant Number mean: 0.00145479 max: 0.0172525 +Time = 0.0009425 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 47 new parcels + +Cloud: sprayCloud + Current number of parcels = 16521 + Current mass in system = 1.37075e-09 + Linear momentum = (2.62848e-11 -1.09136e-08 0) + |Linear momentum| = 1.09136e-08 + Linear kinetic energy = 4.56624e-08 + model1: + number of parcels added = 16539 + mass introduced = 1.41677e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.126, 539.438 + Mass transfer phase change = 4.60205e-11 + D10, D32, Dmax (mu) = 51.2749, 83.4804, 150.24 + Liquid penetration 95% mass (m) = 0.00701248 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00826438, Final residual = 2.8196e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0128397, Final residual = 3.75972e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00176896, Final residual = 1.11587e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0026618, Final residual = 1.63216e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00311063, Final residual = 2.13317e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00311062, Final residual = 2.13515e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00208563, Final residual = 9.74341e-08, No Iterations 1 +min/max(T) = 617.881, 1105.54 +GAMG: Solving for p, Initial residual = 0.0562022, Final residual = 4.81207e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.03616e-06, global = 2.99979e-06, cumulative = 0.00105879 +GAMG: Solving for p, Initial residual = 4.49022e-05, Final residual = 4.07872e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00327e-06, global = 3.00298e-06, cumulative = 0.00106179 +smoothSolver: Solving for epsilon, Initial residual = 0.000898596, Final residual = 1.26073e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00202763, Final residual = 3.31064e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.090239 s +other Time = 0 s +rho Equations = 0.000167 s +U Equations = 0.001215 s +Y Equations = 0.00218137 s +E Equations = 0.000512 s +p Equations = 0.00175 s +calculate parcels = 45.6697 s +chemistry correctThermo = 0.002021 s +turbulence correct = 0.000818 s +combustion correct(in Y) = 0.0813776 s +percentage of chemistry = 90.1801 % +percentage of rho/U/Y/E = 4.5162 % +========Time details of each equation======= +rhoEqn Time = 0.000289 s +rhoEqn assamble = 0.000228 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001214 s +UEqn assamble = 0.000687 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000527 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001526 s +YEqn assamble = 0.000557 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000104 s +YEqn correct boundary = 0 s +EEqn Time = 0.000392 s +EEqn assamble = 0.000299 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 79.47 s ClockTime = 80 s +Courant Number mean: 0.00147739 max: 0.0172602 +Time = 0.000945 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 69 new parcels + +Cloud: sprayCloud + Current number of parcels = 16590 + Current mass in system = 1.37384e-09 + Linear momentum = (2.6764e-11 -1.0925e-08 0) + |Linear momentum| = 1.0925e-08 + Linear kinetic energy = 4.56504e-08 + model1: + number of parcels added = 16608 + mass introduced = 1.42012e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.123, 539.271 + Mass transfer phase change = 4.62811e-11 + D10, D32, Dmax (mu) = 51.2724, 83.5082, 150.248 + Liquid penetration 95% mass (m) = 0.00702716 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00825034, Final residual = 2.84853e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0129266, Final residual = 3.79535e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00178692, Final residual = 1.1436e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00267223, Final residual = 1.65571e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00312497, Final residual = 2.15488e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00312496, Final residual = 2.15688e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00209546, Final residual = 9.87505e-08, No Iterations 1 +min/max(T) = 618.277, 1110 +GAMG: Solving for p, Initial residual = 0.0558563, Final residual = 5.89456e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.03669e-06, global = 2.99977e-06, cumulative = 0.00106479 +GAMG: Solving for p, Initial residual = 5.56384e-05, Final residual = 5.87138e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.0034e-06, global = 3.00303e-06, cumulative = 0.00106779 +smoothSolver: Solving for epsilon, Initial residual = 0.000900278, Final residual = 1.26289e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00202483, Final residual = 3.3165e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103059 s +other Time = 1e-06 s +rho Equations = 0.000216 s +U Equations = 0.001175 s +Y Equations = 0.00239288 s +E Equations = 0.000634 s +p Equations = 0.002093 s +calculate parcels = 45.9281 s +chemistry correctThermo = 0.002793 s +turbulence correct = 0.000988 s +combustion correct(in Y) = 0.0925461 s +percentage of chemistry = 89.7992 % +percentage of rho/U/Y/E = 4.28675 % +========Time details of each equation======= +rhoEqn Time = 0.000365 s +rhoEqn assamble = 0.00029 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001175 s +UEqn assamble = 0.00067 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000505 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001737 s +YEqn assamble = 0.000631 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000172 s +YEqn correct boundary = 0 s +EEqn Time = 0.00046 s +EEqn assamble = 0.000342 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 79.83 s ClockTime = 80 s +Courant Number mean: 0.00150055 max: 0.0172647 +Time = 0.0009475 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 16641 + Current mass in system = 1.37608e-09 + Linear momentum = (2.68299e-11 -1.09303e-08 0) + |Linear momentum| = 1.09303e-08 + Linear kinetic energy = 4.56164e-08 + model1: + number of parcels added = 16659 + mass introduced = 1.42262e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.135, 538.98 + Mass transfer phase change = 4.65416e-11 + D10, D32, Dmax (mu) = 51.186, 83.518, 150.257 + Liquid penetration 95% mass (m) = 0.00704281 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00818521, Final residual = 2.85968e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0130131, Final residual = 3.83179e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00178599, Final residual = 1.14846e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00268282, Final residual = 1.67423e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00313946, Final residual = 2.17689e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00313945, Final residual = 2.17891e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00210391, Final residual = 9.93589e-08, No Iterations 1 +min/max(T) = 618.699, 1114.49 +GAMG: Solving for p, Initial residual = 0.0554518, Final residual = 5.20125e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.0374e-06, global = 2.99924e-06, cumulative = 0.00107079 +GAMG: Solving for p, Initial residual = 4.86081e-05, Final residual = 4.2661e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00312e-06, global = 3.00283e-06, cumulative = 0.00107379 +smoothSolver: Solving for epsilon, Initial residual = 0.00090184, Final residual = 1.26475e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00202193, Final residual = 3.32224e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.084912 s +other Time = 1e-06 s +rho Equations = 0.000169 s +U Equations = 0.001162 s +Y Equations = 0.00249006 s +E Equations = 0.000603 s +p Equations = 0.002054 s +calculate parcels = 46.183 s +chemistry correctThermo = 0.002887 s +turbulence correct = 0.001022 s +combustion correct(in Y) = 0.0743179 s +percentage of chemistry = 87.5235 % +percentage of rho/U/Y/E = 5.21017 % +========Time details of each equation======= +rhoEqn Time = 0.000313 s +rhoEqn assamble = 0.000249 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001161 s +UEqn assamble = 0.000663 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000498 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001798 s +YEqn assamble = 0.000662 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000153 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 80.17 s ClockTime = 81 s +Courant Number mean: 0.00152427 max: 0.0172711 +Time = 0.00095 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 47 new parcels + +Cloud: sprayCloud + Current number of parcels = 16688 + Current mass in system = 1.37813e-09 + Linear momentum = (2.67718e-11 -1.09343e-08 0) + |Linear momentum| = 1.09343e-08 + Linear kinetic energy = 4.55782e-08 + model1: + number of parcels added = 16706 + mass introduced = 1.42493e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.136, 538.524 + Mass transfer phase change = 4.68021e-11 + D10, D32, Dmax (mu) = 51.1624, 83.5353, 150.266 + Liquid penetration 95% mass (m) = 0.00705664 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00813966, Final residual = 2.89349e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0130983, Final residual = 3.86818e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00178037, Final residual = 1.15213e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00269307, Final residual = 1.6937e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00315338, Final residual = 2.19994e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00315337, Final residual = 2.202e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00211112, Final residual = 1.00018e-07, No Iterations 1 +min/max(T) = 619.143, 1119.01 +GAMG: Solving for p, Initial residual = 0.0550753, Final residual = 5.28672e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.04065e-06, global = 2.99891e-06, cumulative = 0.00107679 +GAMG: Solving for p, Initial residual = 4.90994e-05, Final residual = 3.82451e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00286e-06, global = 3.00256e-06, cumulative = 0.0010798 +smoothSolver: Solving for epsilon, Initial residual = 0.000903335, Final residual = 1.26606e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00201867, Final residual = 3.32784e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09278 s +other Time = 0 s +rho Equations = 0.000172 s +U Equations = 0.001198 s +Y Equations = 0.00243178 s +E Equations = 0.00061 s +p Equations = 0.002643 s +calculate parcels = 46.4286 s +chemistry correctThermo = 0.002802 s +turbulence correct = 0.001037 s +combustion correct(in Y) = 0.0816392 s +percentage of chemistry = 87.9923 % +percentage of rho/U/Y/E = 4.7551 % +========Time details of each equation======= +rhoEqn Time = 0.000383 s +rhoEqn assamble = 0.000294 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001198 s +UEqn assamble = 0.000678 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00052 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001784 s +YEqn assamble = 0.000673 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000166 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 80.51 s ClockTime = 81 s +Courant Number mean: 0.00154853 max: 0.0172749 +Time = 0.0009525 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 39 new parcels + +Cloud: sprayCloud + Current number of parcels = 16727 + Current mass in system = 1.37979e-09 + Linear momentum = (2.68812e-11 -1.09355e-08 0) + |Linear momentum| = 1.09356e-08 + Linear kinetic energy = 4.55302e-08 + model1: + number of parcels added = 16745 + mass introduced = 1.42685e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.131, 537.804 + Mass transfer phase change = 4.70626e-11 + D10, D32, Dmax (mu) = 51.1138, 83.5441, 150.274 + Liquid penetration 95% mass (m) = 0.0070722 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00811403, Final residual = 2.95459e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0131802, Final residual = 3.90197e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00177571, Final residual = 1.1537e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00270365, Final residual = 1.71378e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00316754, Final residual = 2.22283e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00316753, Final residual = 2.22491e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00212034, Final residual = 1.00562e-07, No Iterations 1 +min/max(T) = 619.604, 1123.56 +GAMG: Solving for p, Initial residual = 0.0546904, Final residual = 4.57201e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.03707e-06, global = 2.99901e-06, cumulative = 0.0010828 +GAMG: Solving for p, Initial residual = 4.30714e-05, Final residual = 3.78576e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00296e-06, global = 3.00264e-06, cumulative = 0.0010858 +smoothSolver: Solving for epsilon, Initial residual = 0.00090536, Final residual = 1.26694e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00201527, Final residual = 3.33517e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.098032 s +other Time = 0 s +rho Equations = 0.000172 s +U Equations = 0.001311 s +Y Equations = 0.00240052 s +E Equations = 0.000614 s +p Equations = 0.002007 s +calculate parcels = 46.7038 s +chemistry correctThermo = 0.002799 s +turbulence correct = 0.001032 s +combustion correct(in Y) = 0.0874635 s +percentage of chemistry = 89.2193 % +percentage of rho/U/Y/E = 4.58781 % +========Time details of each equation======= +rhoEqn Time = 0.000314 s +rhoEqn assamble = 0.000249 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001309 s +UEqn assamble = 0.000799 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00051 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001763 s +YEqn assamble = 0.000663 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00018 s +YEqn correct boundary = 0 s +EEqn Time = 0.000454 s +EEqn assamble = 0.000329 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000125 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 80.88 s ClockTime = 81 s +Courant Number mean: 0.0015733 max: 0.0172765 +Time = 0.000955 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 16771 + Current mass in system = 1.38169e-09 + Linear momentum = (2.72309e-11 -1.09387e-08 0) + |Linear momentum| = 1.09387e-08 + Linear kinetic energy = 4.54901e-08 + model1: + number of parcels added = 16789 + mass introduced = 1.42901e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.124, 536.685 + Mass transfer phase change = 4.73232e-11 + D10, D32, Dmax (mu) = 51.113, 83.5673, 150.282 + Liquid penetration 95% mass (m) = 0.00708695 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00808331, Final residual = 2.98853e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0132505, Final residual = 3.93149e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00177668, Final residual = 1.1796e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00271415, Final residual = 1.73422e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0031813, Final residual = 2.24633e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00318128, Final residual = 2.24844e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00213088, Final residual = 1.0181e-07, No Iterations 1 +min/max(T) = 620.068, 1128.11 +GAMG: Solving for p, Initial residual = 0.0543013, Final residual = 4.9929e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.03982e-06, global = 2.99935e-06, cumulative = 0.0010888 +GAMG: Solving for p, Initial residual = 4.75658e-05, Final residual = 4.42299e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00341e-06, global = 3.00303e-06, cumulative = 0.0010918 +smoothSolver: Solving for epsilon, Initial residual = 0.000907731, Final residual = 1.268e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00201217, Final residual = 3.34354e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.069263 s +other Time = 0 s +rho Equations = 0.000155 s +U Equations = 0.001211 s +Y Equations = 0.0021795 s +E Equations = 0.000497 s +p Equations = 0.001653 s +calculate parcels = 46.9837 s +chemistry correctThermo = 0.002004 s +turbulence correct = 0.000822 s +combustion correct(in Y) = 0.0605545 s +percentage of chemistry = 87.4269 % +percentage of rho/U/Y/E = 5.83646 % +========Time details of each equation======= +rhoEqn Time = 0.000274 s +rhoEqn assamble = 0.000217 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001211 s +UEqn assamble = 0.000778 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000433 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001606 s +YEqn assamble = 0.000551 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000132 s +YEqn correct boundary = 0 s +EEqn Time = 0.000373 s +EEqn assamble = 0.00028 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 81.23 s ClockTime = 82 s +Courant Number mean: 0.00159859 max: 0.0172936 +Time = 0.0009575 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 67 new parcels + +Cloud: sprayCloud + Current number of parcels = 16838 + Current mass in system = 1.38472e-09 + Linear momentum = (2.65583e-11 -1.09504e-08 0) + |Linear momentum| = 1.09504e-08 + Linear kinetic energy = 4.54831e-08 + model1: + number of parcels added = 16856 + mass introduced = 1.4323e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.127, 535.047 + Mass transfer phase change = 4.75838e-11 + D10, D32, Dmax (mu) = 51.1197, 83.6068, 150.291 + Liquid penetration 95% mass (m) = 0.00710407 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00802742, Final residual = 2.99548e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.013316, Final residual = 3.96146e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0017763, Final residual = 1.19937e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00272579, Final residual = 1.75429e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00319643, Final residual = 2.26907e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00319642, Final residual = 2.27122e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0021419, Final residual = 1.02697e-07, No Iterations 1 +min/max(T) = 620.546, 1132.68 +GAMG: Solving for p, Initial residual = 0.0539245, Final residual = 5.25706e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.04284e-06, global = 3.0001e-06, cumulative = 0.0010948 +GAMG: Solving for p, Initial residual = 4.99224e-05, Final residual = 5.1727e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00414e-06, global = 3.00377e-06, cumulative = 0.0010978 +smoothSolver: Solving for epsilon, Initial residual = 0.000911004, Final residual = 1.2689e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00200927, Final residual = 3.35252e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.07493 s +other Time = 0 s +rho Equations = 0.000162 s +U Equations = 0.001121 s +Y Equations = 0.00207839 s +E Equations = 0.00049 s +p Equations = 0.004329 s +calculate parcels = 47.1888 s +chemistry correctThermo = 0.002941 s +turbulence correct = 0.001584 s +combustion correct(in Y) = 0.0620086 s +percentage of chemistry = 82.7554 % +percentage of rho/U/Y/E = 5.13998 % +========Time details of each equation======= +rhoEqn Time = 0.000473 s +rhoEqn assamble = 0.000368 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000105 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001119 s +UEqn assamble = 0.000693 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000426 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001459 s +YEqn assamble = 0.000535 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.9e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000369 s +EEqn assamble = 0.000279 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 81.51 s ClockTime = 82 s +Courant Number mean: 0.00162448 max: 0.0172992 +Time = 0.00096 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 47 new parcels + +Cloud: sprayCloud + Current number of parcels = 16885 + Current mass in system = 1.38679e-09 + Linear momentum = (2.67208e-11 -1.0955e-08 0) + |Linear momentum| = 1.0955e-08 + Linear kinetic energy = 4.54497e-08 + model1: + number of parcels added = 16903 + mass introduced = 1.43463e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.123, 532.842 + Mass transfer phase change = 4.78445e-11 + D10, D32, Dmax (mu) = 51.0657, 83.6203, 150.299 + Liquid penetration 95% mass (m) = 0.00711909 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00798872, Final residual = 2.99788e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0133895, Final residual = 3.99561e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00177515, Final residual = 1.19541e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00273763, Final residual = 1.77085e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00321159, Final residual = 2.2938e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00321158, Final residual = 2.29598e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00215133, Final residual = 1.02988e-07, No Iterations 1 +min/max(T) = 621.042, 1137.24 +GAMG: Solving for p, Initial residual = 0.0535475, Final residual = 5.8476e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.0496e-06, global = 3.00168e-06, cumulative = 0.00110081 +GAMG: Solving for p, Initial residual = 5.59506e-05, Final residual = 7.17277e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00563e-06, global = 3.00512e-06, cumulative = 0.00110381 +smoothSolver: Solving for epsilon, Initial residual = 0.00091404, Final residual = 1.26967e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00200635, Final residual = 3.36332e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.086223 s +other Time = 0 s +rho Equations = 0.00015 s +U Equations = 0.000986 s +Y Equations = 0.00246518 s +E Equations = 0.000638 s +p Equations = 0.002492 s +calculate parcels = 47.4739 s +chemistry correctThermo = 0.002867 s +turbulence correct = 0.001058 s +combustion correct(in Y) = 0.0753568 s +percentage of chemistry = 87.3976 % +percentage of rho/U/Y/E = 4.91653 % +========Time details of each equation======= +rhoEqn Time = 0.000323 s +rhoEqn assamble = 0.000254 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000986 s +UEqn assamble = 0.000577 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000409 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001903 s +YEqn assamble = 0.000708 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000224 s +YEqn correct boundary = 0 s +EEqn Time = 0.000471 s +EEqn assamble = 0.000356 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 81.88 s ClockTime = 82 s +Courant Number mean: 0.00165094 max: 0.0172962 +Time = 0.0009625 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 41 new parcels + +Cloud: sprayCloud + Current number of parcels = 16926 + Current mass in system = 1.38856e-09 + Linear momentum = (2.64636e-11 -1.09575e-08 0) + |Linear momentum| = 1.09575e-08 + Linear kinetic energy = 4.54084e-08 + model1: + number of parcels added = 16944 + mass introduced = 1.43666e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.13, 530.13 + Mass transfer phase change = 4.81053e-11 + D10, D32, Dmax (mu) = 51.0656, 83.6495, 150.307 + Liquid penetration 95% mass (m) = 0.00713524 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00798051, Final residual = 2.98718e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0134748, Final residual = 4.03293e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00177193, Final residual = 1.20207e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00275096, Final residual = 1.79321e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0032289, Final residual = 2.32054e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00322889, Final residual = 2.32275e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0021586, Final residual = 1.03501e-07, No Iterations 1 +min/max(T) = 621.55, 1141.79 +GAMG: Solving for p, Initial residual = 0.0532369, Final residual = 6.15241e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.05796e-06, global = 3.00216e-06, cumulative = 0.00110681 +GAMG: Solving for p, Initial residual = 5.81019e-05, Final residual = 6.31486e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00635e-06, global = 3.00577e-06, cumulative = 0.00110982 +smoothSolver: Solving for epsilon, Initial residual = 0.000916566, Final residual = 1.27217e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00200372, Final residual = 3.37493e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100085 s +other Time = 0 s +rho Equations = 0.000176 s +U Equations = 0.001168 s +Y Equations = 0.00223014 s +E Equations = 0.000508 s +p Equations = 0.001902 s +calculate parcels = 47.7762 s +chemistry correctThermo = 0.002012 s +turbulence correct = 0.000841 s +combustion correct(in Y) = 0.0910379 s +percentage of chemistry = 90.9605 % +percentage of rho/U/Y/E = 4.07868 % +========Time details of each equation======= +rhoEqn Time = 0.000304 s +rhoEqn assamble = 0.000242 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001168 s +UEqn assamble = 0.000663 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000505 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001594 s +YEqn assamble = 0.000579 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000113 s +YEqn correct boundary = 0 s +EEqn Time = 0.000384 s +EEqn assamble = 0.000289 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 82.28 s ClockTime = 83 s +Courant Number mean: 0.00167802 max: 0.0173027 +Time = 0.000965 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 16969 + Current mass in system = 1.39046e-09 + Linear momentum = (2.62482e-11 -1.0961e-08 0) + |Linear momentum| = 1.0961e-08 + Linear kinetic energy = 4.53717e-08 + model1: + number of parcels added = 16988 + mass introduced = 1.43883e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.131, 527.125 + Mass transfer phase change = 4.8367e-11 + D10, D32, Dmax (mu) = 51.7785, 83.6691, 150.315 + Liquid penetration 95% mass (m) = 0.00715052 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00815392, Final residual = 3.03395e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.013553, Final residual = 4.07382e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00177785, Final residual = 1.23794e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00276619, Final residual = 1.82023e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00324669, Final residual = 2.34969e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00324668, Final residual = 2.35196e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00216988, Final residual = 1.04894e-07, No Iterations 1 +min/max(T) = 622.072, 1146.31 +GAMG: Solving for p, Initial residual = 0.0529132, Final residual = 6.11172e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.06914e-06, global = 3.01187e-06, cumulative = 0.00111283 +GAMG: Solving for p, Initial residual = 5.6326e-05, Final residual = 5.49947e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.01647e-06, global = 3.01597e-06, cumulative = 0.00111585 +smoothSolver: Solving for epsilon, Initial residual = 0.000919291, Final residual = 1.2752e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0020014, Final residual = 3.3864e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.11635 s +other Time = 0 s +rho Equations = 0.000237 s +U Equations = 0.001643 s +Y Equations = 0.00261916 s +E Equations = 0.000603 s +p Equations = 0.002004 s +calculate parcels = 48.0418 s +chemistry correctThermo = 0.002782 s +turbulence correct = 0.001038 s +combustion correct(in Y) = 0.10516 s +percentage of chemistry = 90.3823 % +percentage of rho/U/Y/E = 4.38518 % +========Time details of each equation======= +rhoEqn Time = 0.000376 s +rhoEqn assamble = 0.000288 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001642 s +UEqn assamble = 0.000875 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000767 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.0015 s +YEqn assamble = 0.000652 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -6.9e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000451 s +EEqn assamble = 0.000338 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 82.67 s ClockTime = 83 s +Courant Number mean: 0.00170576 max: 0.0173093 +Time = 0.0009675 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 17015 + Current mass in system = 1.39245e-09 + Linear momentum = (2.65048e-11 -1.09653e-08 0) + |Linear momentum| = 1.09653e-08 + Linear kinetic energy = 4.5338e-08 + model1: + number of parcels added = 17034 + mass introduced = 1.44108e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.142, 524.656 + Mass transfer phase change = 4.86277e-11 + D10, D32, Dmax (mu) = 51.7753, 83.6898, 150.323 + Liquid penetration 95% mass (m) = 0.00716387 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00826937, Final residual = 3.08611e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0136456, Final residual = 4.12223e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00176444, Final residual = 1.22989e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00277862, Final residual = 1.84067e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00326482, Final residual = 2.38008e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00326481, Final residual = 2.38239e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00217473, Final residual = 1.05501e-07, No Iterations 1 +min/max(T) = 622.614, 1150.8 +GAMG: Solving for p, Initial residual = 0.0526258, Final residual = 6.4745e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.06336e-06, global = 3.00055e-06, cumulative = 0.00111885 +GAMG: Solving for p, Initial residual = 6.02582e-05, Final residual = 4.92408e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00523e-06, global = 3.00476e-06, cumulative = 0.00112185 +smoothSolver: Solving for epsilon, Initial residual = 0.000921812, Final residual = 1.27781e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00199898, Final residual = 3.39789e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.087191 s +other Time = 0 s +rho Equations = 0.000174 s +U Equations = 0.001319 s +Y Equations = 0.00236866 s +E Equations = 0.00062 s +p Equations = 0.00216 s +calculate parcels = 48.3376 s +chemistry correctThermo = 0.002799 s +turbulence correct = 0.001047 s +combustion correct(in Y) = 0.0764883 s +percentage of chemistry = 87.725 % +percentage of rho/U/Y/E = 5.14005 % +========Time details of each equation======= +rhoEqn Time = 0.000332 s +rhoEqn assamble = 0.000261 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001319 s +UEqn assamble = 0.00076 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000559 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001666 s +YEqn assamble = 0.000626 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000131 s +YEqn correct boundary = 0 s +EEqn Time = 0.000465 s +EEqn assamble = 0.000352 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 83.05 s ClockTime = 84 s +Courant Number mean: 0.00173418 max: 0.017313 +Time = 0.00097 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 53 new parcels + +Cloud: sprayCloud + Current number of parcels = 17067 + Current mass in system = 1.39478e-09 + Linear momentum = (2.63188e-11 -1.09721e-08 0) + |Linear momentum| = 1.09721e-08 + Linear kinetic energy = 4.53144e-08 + model1: + number of parcels added = 17087 + mass introduced = 1.44367e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.144, 524.892 + Mass transfer phase change = 4.88894e-11 + D10, D32, Dmax (mu) = 52.8508, 83.7156, 150.331 + Liquid penetration 95% mass (m) = 0.00718085 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00855036, Final residual = 3.19307e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0137458, Final residual = 4.1769e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00177065, Final residual = 1.25905e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00279461, Final residual = 1.86835e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00328281, Final residual = 2.4101e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00328279, Final residual = 2.41244e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00218399, Final residual = 1.07027e-07, No Iterations 1 +min/max(T) = 623.179, 1155.23 +GAMG: Solving for p, Initial residual = 0.0523549, Final residual = 6.91179e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.07713e-06, global = 3.01322e-06, cumulative = 0.00112487 +GAMG: Solving for p, Initial residual = 6.47659e-05, Final residual = 6.34601e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.01768e-06, global = 3.01707e-06, cumulative = 0.00112788 +smoothSolver: Solving for epsilon, Initial residual = 0.000924635, Final residual = 1.28133e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00199749, Final residual = 3.41125e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097477 s +other Time = 0 s +rho Equations = 0.00017 s +U Equations = 0.001203 s +Y Equations = 0.00226395 s +E Equations = 0.000492 s +p Equations = 0.001678 s +calculate parcels = 48.6253 s +chemistry correctThermo = 0.001965 s +turbulence correct = 0.000858 s +combustion correct(in Y) = 0.0886501 s +percentage of chemistry = 90.9446 % +percentage of rho/U/Y/E = 4.23582 % +========Time details of each equation======= +rhoEqn Time = 0.000288 s +rhoEqn assamble = 0.000228 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001202 s +UEqn assamble = 0.000662 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00054 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001608 s +YEqn assamble = 0.000589 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000118 s +YEqn correct boundary = 0 s +EEqn Time = 0.00037 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 83.43 s ClockTime = 84 s +Courant Number mean: 0.00176348 max: 0.017317 +Time = 0.0009725 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 56 new parcels + +Cloud: sprayCloud + Current number of parcels = 17123 + Current mass in system = 1.39725e-09 + Linear momentum = (2.65385e-11 -1.09801e-08 0) + |Linear momentum| = 1.09801e-08 + Linear kinetic energy = 4.52954e-08 + model1: + number of parcels added = 17143 + mass introduced = 1.4464e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.136, 525.654 + Mass transfer phase change = 4.91499e-11 + D10, D32, Dmax (mu) = 52.8634, 83.7466, 150.339 + Liquid penetration 95% mass (m) = 0.00719624 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0087348, Final residual = 3.28544e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0138551, Final residual = 4.23305e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0017693, Final residual = 1.27283e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00280719, Final residual = 1.88772e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0033014, Final residual = 2.44175e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00330139, Final residual = 2.44413e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00219342, Final residual = 1.07565e-07, No Iterations 1 +min/max(T) = 623.757, 1159.58 +GAMG: Solving for p, Initial residual = 0.0520298, Final residual = 6.2231e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.05958e-06, global = 2.99731e-06, cumulative = 0.00113088 +GAMG: Solving for p, Initial residual = 5.68305e-05, Final residual = 4.58887e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00296e-06, global = 3.00251e-06, cumulative = 0.00113388 +smoothSolver: Solving for epsilon, Initial residual = 0.000927926, Final residual = 1.28588e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00199759, Final residual = 3.42592e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.068904 s +other Time = 1e-06 s +rho Equations = 0.000178 s +U Equations = 0.001038 s +Y Equations = 0.00218942 s +E Equations = 0.000502 s +p Equations = 0.001789 s +calculate parcels = 48.8801 s +chemistry correctThermo = 0.001969 s +turbulence correct = 0.000914 s +combustion correct(in Y) = 0.0601356 s +percentage of chemistry = 87.2744 % +percentage of rho/U/Y/E = 5.67082 % +========Time details of each equation======= +rhoEqn Time = 0.000324 s +rhoEqn assamble = 0.000248 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001037 s +UEqn assamble = 0.000628 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000409 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001627 s +YEqn assamble = 0.00058 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000148 s +YEqn correct boundary = 0 s +EEqn Time = 0.000375 s +EEqn assamble = 0.000281 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 83.76 s ClockTime = 84 s +Courant Number mean: 0.00179365 max: 0.0173298 +Time = 0.000975 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 42 new parcels + +Cloud: sprayCloud + Current number of parcels = 17165 + Current mass in system = 1.39904e-09 + Linear momentum = (2.6042e-11 -1.09831e-08 0) + |Linear momentum| = 1.09831e-08 + Linear kinetic energy = 4.52582e-08 + model1: + number of parcels added = 17185 + mass introduced = 1.44845e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.14, 526.437 + Mass transfer phase change = 4.94105e-11 + D10, D32, Dmax (mu) = 52.8629, 83.7591, 150.348 + Liquid penetration 95% mass (m) = 0.00721172 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00900057, Final residual = 3.38989e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0139679, Final residual = 4.29258e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00177212, Final residual = 1.29745e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00282197, Final residual = 1.91201e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00331963, Final residual = 2.47419e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00331962, Final residual = 2.47661e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00220508, Final residual = 1.08569e-07, No Iterations 1 +min/max(T) = 624.294, 1163.84 +GAMG: Solving for p, Initial residual = 0.0517422, Final residual = 5.65001e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.05679e-06, global = 2.99812e-06, cumulative = 0.00113688 +GAMG: Solving for p, Initial residual = 5.18166e-05, Final residual = 3.14184e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.0033e-06, global = 3.00298e-06, cumulative = 0.00113988 +smoothSolver: Solving for epsilon, Initial residual = 0.000932398, Final residual = 1.29426e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00199915, Final residual = 3.44286e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.088831 s +other Time = 0 s +rho Equations = 0.000175 s +U Equations = 0.00121 s +Y Equations = 0.0024465 s +E Equations = 0.000627 s +p Equations = 0.002228 s +calculate parcels = 49.1112 s +chemistry correctThermo = 0.002896 s +turbulence correct = 0.000988 s +combustion correct(in Y) = 0.0780505 s +percentage of chemistry = 87.864 % +percentage of rho/U/Y/E = 5.01908 % +========Time details of each equation======= +rhoEqn Time = 0.00033 s +rhoEqn assamble = 0.00026 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001208 s +UEqn assamble = 0.000677 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000531 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001799 s +YEqn assamble = 0.00068 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000191 s +YEqn correct boundary = 0 s +EEqn Time = 0.000476 s +EEqn assamble = 0.000355 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000121 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 84.08 s ClockTime = 85 s +Courant Number mean: 0.00182484 max: 0.0173452 +Time = 0.0009775 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 43 new parcels + +Cloud: sprayCloud + Current number of parcels = 17208 + Current mass in system = 1.40087e-09 + Linear momentum = (2.64903e-11 -1.09864e-08 0) + |Linear momentum| = 1.09864e-08 + Linear kinetic energy = 4.52227e-08 + model1: + number of parcels added = 17228 + mass introduced = 1.45054e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.14, 527.238 + Mass transfer phase change = 4.9671e-11 + D10, D32, Dmax (mu) = 52.8621, 83.774, 150.356 + Liquid penetration 95% mass (m) = 0.00722653 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00916854, Final residual = 3.49929e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0140908, Final residual = 4.35519e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00176939, Final residual = 1.30192e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0028369, Final residual = 1.93622e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00333789, Final residual = 2.50643e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00333788, Final residual = 2.50888e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00221607, Final residual = 1.08989e-07, No Iterations 1 +min/max(T) = 624.072, 1169.8 +GAMG: Solving for p, Initial residual = 0.0514408, Final residual = 5.2012e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.05177e-06, global = 2.99843e-06, cumulative = 0.00114288 +GAMG: Solving for p, Initial residual = 4.80799e-05, Final residual = 3.89217e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00373e-06, global = 3.00338e-06, cumulative = 0.00114589 +smoothSolver: Solving for epsilon, Initial residual = 0.000936815, Final residual = 1.30324e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00200077, Final residual = 3.4596e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.088187 s +other Time = 1e-06 s +rho Equations = 0.000144 s +U Equations = 0.001055 s +Y Equations = 0.0020103 s +E Equations = 0.000514 s +p Equations = 0.00167 s +calculate parcels = 49.3858 s +chemistry correctThermo = 0.002036 s +turbulence correct = 0.000807 s +combustion correct(in Y) = 0.0797767 s +percentage of chemistry = 90.4631 % +percentage of rho/U/Y/E = 4.22206 % +========Time details of each equation======= +rhoEqn Time = 0.00027 s +rhoEqn assamble = 0.000217 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001054 s +UEqn assamble = 0.000557 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000497 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001457 s +YEqn assamble = 0.000525 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000157 s +YEqn correct boundary = 0 s +EEqn Time = 0.00039 s +EEqn assamble = 0.000288 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000102 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 84.44 s ClockTime = 85 s +Courant Number mean: 0.00185695 max: 0.0173507 +Time = 0.00098 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 53 new parcels + +Cloud: sprayCloud + Current number of parcels = 17261 + Current mass in system = 1.40318e-09 + Linear momentum = (2.66719e-11 -1.09934e-08 0) + |Linear momentum| = 1.09934e-08 + Linear kinetic energy = 4.5201e-08 + model1: + number of parcels added = 17281 + mass introduced = 1.45311e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.13, 528.053 + Mass transfer phase change = 4.99317e-11 + D10, D32, Dmax (mu) = 52.8681, 83.7969, 150.364 + Liquid penetration 95% mass (m) = 0.00724152 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.009231, Final residual = 3.58875e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.014217, Final residual = 4.41499e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00176905, Final residual = 1.31947e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00285209, Final residual = 1.9626e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0033561, Final residual = 2.5397e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00335609, Final residual = 2.5422e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.002228, Final residual = 1.09822e-07, No Iterations 1 +min/max(T) = 623.874, 1178.58 +GAMG: Solving for p, Initial residual = 0.0511396, Final residual = 5.59667e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.05551e-06, global = 2.99907e-06, cumulative = 0.00114888 +GAMG: Solving for p, Initial residual = 5.18187e-05, Final residual = 4.91993e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00499e-06, global = 3.00458e-06, cumulative = 0.00115189 +smoothSolver: Solving for epsilon, Initial residual = 0.000940771, Final residual = 1.31308e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00200232, Final residual = 3.47618e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.088985 s +other Time = 0 s +rho Equations = 0.000176 s +U Equations = 0.001143 s +Y Equations = 0.00217198 s +E Equations = 0.000497 s +p Equations = 0.001677 s +calculate parcels = 49.6798 s +chemistry correctThermo = 0.002035 s +turbulence correct = 0.000867 s +combustion correct(in Y) = 0.080215 s +percentage of chemistry = 90.1444 % +percentage of rho/U/Y/E = 4.48163 % +========Time details of each equation======= +rhoEqn Time = 0.000293 s +rhoEqn assamble = 0.000232 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001142 s +UEqn assamble = 0.000649 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000493 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001529 s +YEqn assamble = 0.000532 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00015 s +YEqn correct boundary = 0 s +EEqn Time = 0.000376 s +EEqn assamble = 0.000281 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 84.82 s ClockTime = 85 s +Courant Number mean: 0.00188993 max: 0.0173585 +Time = 0.0009825 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 40 new parcels + +Cloud: sprayCloud + Current number of parcels = 17301 + Current mass in system = 1.40485e-09 + Linear momentum = (2.69725e-11 -1.09957e-08 0) + |Linear momentum| = 1.09958e-08 + Linear kinetic energy = 4.51627e-08 + model1: + number of parcels added = 17321 + mass introduced = 1.45504e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.132, 528.876 + Mass transfer phase change = 5.01925e-11 + D10, D32, Dmax (mu) = 52.8643, 83.8149, 150.372 + Liquid penetration 95% mass (m) = 0.0072576 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00915729, Final residual = 3.61861e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.014345, Final residual = 4.47364e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00176504, Final residual = 1.31664e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00286707, Final residual = 1.98817e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00337385, Final residual = 2.57261e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00337384, Final residual = 2.57514e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00223982, Final residual = 1.09969e-07, No Iterations 1 +min/max(T) = 623.69, 1187.64 +GAMG: Solving for p, Initial residual = 0.0508383, Final residual = 5.12273e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.05611e-06, global = 2.99992e-06, cumulative = 0.00115489 +GAMG: Solving for p, Initial residual = 4.85497e-05, Final residual = 3.53073e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00605e-06, global = 3.00571e-06, cumulative = 0.00115789 +smoothSolver: Solving for epsilon, Initial residual = 0.00094428, Final residual = 1.32326e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00200363, Final residual = 3.49211e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.099416 s +other Time = 1e-06 s +rho Equations = 0.000176 s +U Equations = 0.001322 s +Y Equations = 0.00311466 s +E Equations = 0.000615 s +p Equations = 0.001752 s +calculate parcels = 49.9867 s +chemistry correctThermo = 0.002762 s +turbulence correct = 0.000882 s +combustion correct(in Y) = 0.0885913 s +percentage of chemistry = 89.1118 % +percentage of rho/U/Y/E = 5.25837 % +========Time details of each equation======= +rhoEqn Time = 0.000293 s +rhoEqn assamble = 0.000235 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00132 s +UEqn assamble = 0.000703 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000617 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001248 s +YEqn assamble = 0.000688 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -0.000396 s +YEqn correct boundary = 0 s +EEqn Time = 0.000454 s +EEqn assamble = 0.00034 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 85.23 s ClockTime = 86 s +Courant Number mean: 0.0019237 max: 0.0173541 +Time = 0.000985 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 43 new parcels + +Cloud: sprayCloud + Current number of parcels = 17344 + Current mass in system = 1.40666e-09 + Linear momentum = (2.72264e-11 -1.09992e-08 0) + |Linear momentum| = 1.09992e-08 + Linear kinetic energy = 4.51286e-08 + model1: + number of parcels added = 17364 + mass introduced = 1.45711e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.175, 529.616 + Mass transfer phase change = 5.04534e-11 + D10, D32, Dmax (mu) = 52.8358, 83.8221, 150.38 + Liquid penetration 95% mass (m) = 0.00727382 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00905237, Final residual = 3.64696e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0144671, Final residual = 4.52974e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0017658, Final residual = 1.31129e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0028819, Final residual = 2.01132e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00339115, Final residual = 2.60535e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00339114, Final residual = 2.60791e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00225204, Final residual = 1.10329e-07, No Iterations 1 +min/max(T) = 623.519, 1197 +GAMG: Solving for p, Initial residual = 0.0505321, Final residual = 6.00677e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.06769e-06, global = 3.00106e-06, cumulative = 0.0011609 +GAMG: Solving for p, Initial residual = 5.66265e-05, Final residual = 4.20209e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00737e-06, global = 3.00689e-06, cumulative = 0.0011639 +smoothSolver: Solving for epsilon, Initial residual = 0.00094756, Final residual = 1.33484e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00200456, Final residual = 3.50724e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100207 s +other Time = 0 s +rho Equations = 0.000203 s +U Equations = 0.001182 s +Y Equations = 0.00240221 s +E Equations = 0.000603 s +p Equations = 0.001704 s +calculate parcels = 50.2642 s +chemistry correctThermo = 0.00251 s +turbulence correct = 0.000895 s +combustion correct(in Y) = 0.0904898 s +percentage of chemistry = 90.3029 % +percentage of rho/U/Y/E = 4.38114 % +========Time details of each equation======= +rhoEqn Time = 0.000321 s +rhoEqn assamble = 0.000254 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001182 s +UEqn assamble = 0.000689 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000493 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001765 s +YEqn assamble = 0.000639 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000185 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 85.61 s ClockTime = 86 s +Courant Number mean: 0.00195819 max: 0.0173657 +Time = 0.0009875 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 56 new parcels + +Cloud: sprayCloud + Current number of parcels = 17400 + Current mass in system = 1.40908e-09 + Linear momentum = (2.71457e-11 -1.10072e-08 0) + |Linear momentum| = 1.10072e-08 + Linear kinetic energy = 4.5112e-08 + model1: + number of parcels added = 17420 + mass introduced = 1.4598e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.124, 530.16 + Mass transfer phase change = 5.07144e-11 + D10, D32, Dmax (mu) = 52.7816, 83.8384, 150.389 + Liquid penetration 95% mass (m) = 0.00728997 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00888654, Final residual = 3.6563e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0145907, Final residual = 4.58717e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00176596, Final residual = 1.3045e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00289638, Final residual = 2.03391e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00340788, Final residual = 2.63841e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00340787, Final residual = 2.64103e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00226472, Final residual = 1.10895e-07, No Iterations 1 +min/max(T) = 623.368, 1206.65 +GAMG: Solving for p, Initial residual = 0.0502222, Final residual = 5.76398e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.06933e-06, global = 3.00191e-06, cumulative = 0.0011669 +GAMG: Solving for p, Initial residual = 5.43942e-05, Final residual = 3.82325e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.00843e-06, global = 3.00798e-06, cumulative = 0.00116991 +smoothSolver: Solving for epsilon, Initial residual = 0.000950957, Final residual = 1.34643e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00200529, Final residual = 3.52467e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.099149 s +other Time = 0 s +rho Equations = 0.000171 s +U Equations = 0.001177 s +Y Equations = 0.00268197 s +E Equations = 0.00069 s +p Equations = 0.002186 s +calculate parcels = 50.5309 s +chemistry correctThermo = 0.0028 s +turbulence correct = 0.001105 s +combustion correct(in Y) = 0.088139 s +percentage of chemistry = 88.8955 % +percentage of rho/U/Y/E = 4.76048 % +========Time details of each equation======= +rhoEqn Time = 0.000344 s +rhoEqn assamble = 0.000274 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001176 s +UEqn assamble = 0.000673 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000503 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002038 s +YEqn assamble = 0.00074 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000215 s +YEqn correct boundary = 0 s +EEqn Time = 0.00051 s +EEqn assamble = 0.000376 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000134 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 85.98 s ClockTime = 86 s +Courant Number mean: 0.00199336 max: 0.0173799 +Time = 0.00099 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 63 new parcels + +Cloud: sprayCloud + Current number of parcels = 17463 + Current mass in system = 1.41184e-09 + Linear momentum = (2.766e-11 -1.10177e-08 0) + |Linear momentum| = 1.10177e-08 + Linear kinetic energy = 4.51051e-08 + model1: + number of parcels added = 17483 + mass introduced = 1.46282e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.133, 530.644 + Mass transfer phase change = 5.09755e-11 + D10, D32, Dmax (mu) = 52.7782, 83.8564, 150.397 + Liquid penetration 95% mass (m) = 0.00730439 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00864575, Final residual = 3.62799e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0147094, Final residual = 4.64454e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00176686, Final residual = 1.30189e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00291061, Final residual = 2.06164e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00342391, Final residual = 2.67191e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00342389, Final residual = 2.67448e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00227685, Final residual = 1.11714e-07, No Iterations 1 +min/max(T) = 623.235, 1216.61 +GAMG: Solving for p, Initial residual = 0.0499166, Final residual = 5.58745e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.0691e-06, global = 3.00356e-06, cumulative = 0.00117292 +GAMG: Solving for p, Initial residual = 5.38091e-05, Final residual = 4.16348e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.01012e-06, global = 3.00961e-06, cumulative = 0.00117593 +smoothSolver: Solving for epsilon, Initial residual = 0.000954138, Final residual = 1.35774e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00200604, Final residual = 3.54159e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.068241 s +other Time = 0 s +rho Equations = 0.000159 s +U Equations = 0.001028 s +Y Equations = 0.00208953 s +E Equations = 0.000488 s +p Equations = 0.00168 s +calculate parcels = 50.7483 s +chemistry correctThermo = 0.001914 s +turbulence correct = 0.000812 s +combustion correct(in Y) = 0.0598895 s +percentage of chemistry = 87.7617 % +percentage of rho/U/Y/E = 5.51653 % +========Time details of each equation======= +rhoEqn Time = 0.000278 s +rhoEqn assamble = 0.000224 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001027 s +UEqn assamble = 0.00059 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000437 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001504 s +YEqn assamble = 0.000529 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000121 s +YEqn correct boundary = 0 s +EEqn Time = 0.000367 s +EEqn assamble = 0.000276 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 86.26 s ClockTime = 87 s +Courant Number mean: 0.00202917 max: 0.0173935 +Time = 0.0009925 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 17512 + Current mass in system = 1.41394e-09 + Linear momentum = (2.75556e-11 -1.10234e-08 0) + |Linear momentum| = 1.10235e-08 + Linear kinetic energy = 4.50808e-08 + model1: + number of parcels added = 17532 + mass introduced = 1.46518e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.141, 531.074 + Mass transfer phase change = 5.12366e-11 + D10, D32, Dmax (mu) = 52.7905, 83.8886, 150.405 + Liquid penetration 95% mass (m) = 0.0073199 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00836329, Final residual = 3.58927e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0148185, Final residual = 4.69772e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00176666, Final residual = 1.30497e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00292415, Final residual = 2.0895e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00343892, Final residual = 2.70674e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00343891, Final residual = 2.70934e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00228846, Final residual = 1.12216e-07, No Iterations 1 +min/max(T) = 623.126, 1226.88 +GAMG: Solving for p, Initial residual = 0.0496079, Final residual = 5.81286e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.07276e-06, global = 3.00437e-06, cumulative = 0.00117893 +GAMG: Solving for p, Initial residual = 5.60155e-05, Final residual = 4.32494e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.01083e-06, global = 3.01029e-06, cumulative = 0.00118194 +smoothSolver: Solving for epsilon, Initial residual = 0.000956925, Final residual = 1.36847e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00200683, Final residual = 3.558e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.093893 s +other Time = 1e-06 s +rho Equations = 0.000168 s +U Equations = 0.001185 s +Y Equations = 0.00216175 s +E Equations = 0.000705 s +p Equations = 0.002113 s +calculate parcels = 51.0257 s +chemistry correctThermo = 0.002864 s +turbulence correct = 0.001018 s +combustion correct(in Y) = 0.0834743 s +percentage of chemistry = 88.9036 % +percentage of rho/U/Y/E = 4.49421 % +========Time details of each equation======= +rhoEqn Time = 0.000321 s +rhoEqn assamble = 0.000255 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001185 s +UEqn assamble = 0.000683 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000502 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001523 s +YEqn assamble = 0.000547 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000155 s +YEqn correct boundary = 0 s +EEqn Time = 0.000511 s +EEqn assamble = 0.000385 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000126 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 86.63 s ClockTime = 87 s +Courant Number mean: 0.00206556 max: 0.0174008 +Time = 0.000995 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 43 new parcels + +Cloud: sprayCloud + Current number of parcels = 17555 + Current mass in system = 1.41574e-09 + Linear momentum = (2.79048e-11 -1.10271e-08 0) + |Linear momentum| = 1.10271e-08 + Linear kinetic energy = 4.50492e-08 + model1: + number of parcels added = 17575 + mass introduced = 1.46724e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.164, 531.446 + Mass transfer phase change = 5.14979e-11 + D10, D32, Dmax (mu) = 52.7944, 83.9125, 150.414 + Liquid penetration 95% mass (m) = 0.00733458 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0081424, Final residual = 3.539e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0149107, Final residual = 4.74731e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00176569, Final residual = 1.31382e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00293685, Final residual = 2.11762e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00345257, Final residual = 2.74103e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00345255, Final residual = 2.74367e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00230056, Final residual = 1.12984e-07, No Iterations 1 +min/max(T) = 623.034, 1237.46 +GAMG: Solving for p, Initial residual = 0.0492956, Final residual = 5.11096e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.06824e-06, global = 3.00546e-06, cumulative = 0.00118495 +GAMG: Solving for p, Initial residual = 4.87167e-05, Final residual = 3.65321e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.01152e-06, global = 3.01106e-06, cumulative = 0.00118796 +smoothSolver: Solving for epsilon, Initial residual = 0.000959597, Final residual = 1.37976e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00200755, Final residual = 3.57366e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.087408 s +other Time = 1e-06 s +rho Equations = 0.000262 s +U Equations = 0.0016 s +Y Equations = 0.00238141 s +E Equations = 0.000962 s +p Equations = 0.003242 s +calculate parcels = 51.3118 s +chemistry correctThermo = 0.006043 s +turbulence correct = 0.00157 s +combustion correct(in Y) = 0.0710966 s +percentage of chemistry = 81.3388 % +percentage of rho/U/Y/E = 5.9553 % +========Time details of each equation======= +rhoEqn Time = 0.000525 s +rhoEqn assamble = 0.000391 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000134 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.0016 s +UEqn assamble = 0.000854 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000746 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00137 s +YEqn assamble = 0.000522 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 5.1e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000721 s +EEqn assamble = 0.000525 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000196 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 87.01 s ClockTime = 87 s +Courant Number mean: 0.00210258 max: 0.0174094 +Time = 0.0009975 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 47 new parcels + +Cloud: sprayCloud + Current number of parcels = 17602 + Current mass in system = 1.41773e-09 + Linear momentum = (2.76942e-11 -1.10322e-08 0) + |Linear momentum| = 1.10322e-08 + Linear kinetic energy = 4.50231e-08 + model1: + number of parcels added = 17622 + mass introduced = 1.46949e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.141, 531.762 + Mass transfer phase change = 5.17592e-11 + D10, D32, Dmax (mu) = 52.7836, 83.9246, 150.422 + Liquid penetration 95% mass (m) = 0.00735002 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0079419, Final residual = 3.50033e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0149971, Final residual = 4.79289e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00176067, Final residual = 1.31749e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00294932, Final residual = 2.14785e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00346564, Final residual = 2.77455e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00346563, Final residual = 2.77722e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00231349, Final residual = 1.14032e-07, No Iterations 1 +min/max(T) = 622.967, 1248.36 +GAMG: Solving for p, Initial residual = 0.0489789, Final residual = 4.95847e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.0699e-06, global = 3.00667e-06, cumulative = 0.00119096 +GAMG: Solving for p, Initial residual = 4.70595e-05, Final residual = 3.86617e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.01276e-06, global = 3.01229e-06, cumulative = 0.00119398 +smoothSolver: Solving for epsilon, Initial residual = 0.000962011, Final residual = 1.38996e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00200886, Final residual = 3.58766e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095586 s +other Time = 0 s +rho Equations = 0.000169 s +U Equations = 0.001201 s +Y Equations = 0.0038414 s +E Equations = 0.000977 s +p Equations = 0.003454 s +calculate parcels = 51.6132 s +chemistry correctThermo = 0.005455 s +turbulence correct = 0.00163 s +combustion correct(in Y) = 0.0786316 s +percentage of chemistry = 82.2627 % +percentage of rho/U/Y/E = 6.47417 % +========Time details of each equation======= +rhoEqn Time = 0.000453 s +rhoEqn assamble = 0.000342 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000111 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001199 s +UEqn assamble = 0.000665 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000534 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.003155 s +YEqn assamble = 0.001081 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000554 s +YEqn correct boundary = 0 s +EEqn Time = 0.000733 s +EEqn assamble = 0.00053 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000203 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 87.4 s ClockTime = 88 s +Courant Number mean: 0.00214029 max: 0.0174188 +Time = 0.001 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 65 new parcels + +Cloud: sprayCloud + Current number of parcels = 17667 + Current mass in system = 1.42057e-09 + Linear momentum = (2.76471e-11 -1.10435e-08 0) + |Linear momentum| = 1.10436e-08 + Linear kinetic energy = 4.50206e-08 + model1: + number of parcels added = 17687 + mass introduced = 1.47259e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.137, 532.026 + Mass transfer phase change = 5.20207e-11 + D10, D32, Dmax (mu) = 52.7999, 83.9655, 150.431 + Liquid penetration 95% mass (m) = 0.00736348 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00774237, Final residual = 3.50154e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0150803, Final residual = 4.83844e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00175575, Final residual = 1.32766e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00296174, Final residual = 2.17831e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00347853, Final residual = 2.80775e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00347852, Final residual = 2.81058e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00232581, Final residual = 1.14849e-07, No Iterations 1 +min/max(T) = 622.928, 1259.58 +GAMG: Solving for p, Initial residual = 0.0486788, Final residual = 5.43981e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.07862e-06, global = 3.00767e-06, cumulative = 0.00119698 +GAMG: Solving for p, Initial residual = 5.13462e-05, Final residual = 5.1569e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.01391e-06, global = 3.01331e-06, cumulative = 0.0012 +smoothSolver: Solving for epsilon, Initial residual = 0.000964158, Final residual = 1.39962e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00201073, Final residual = 3.60141e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.096387 s +other Time = 0 s +rho Equations = 0.000144 s +U Equations = 0.001015 s +Y Equations = 0.00229127 s +E Equations = 0.000587 s +p Equations = 0.002004 s +calculate parcels = 51.8948 s +chemistry correctThermo = 0.002794 s +turbulence correct = 0.00094 s +combustion correct(in Y) = 0.0864457 s +percentage of chemistry = 89.6861 % +percentage of rho/U/Y/E = 4.18861 % +========Time details of each equation======= +rhoEqn Time = 0.000286 s +rhoEqn assamble = 0.000227 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001012 s +UEqn assamble = 0.000582 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00043 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001704 s +YEqn assamble = 0.000621 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000191 s +YEqn correct boundary = 0 s +EEqn Time = 0.000436 s +EEqn assamble = 0.000327 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000109 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 88.08 s ClockTime = 89 s +Courant Number mean: 0.00217877 max: 0.017422 +Time = 0.0010025 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 17717 + Current mass in system = 1.4227e-09 + Linear momentum = (2.82041e-11 -1.10497e-08 0) + |Linear momentum| = 1.10498e-08 + Linear kinetic energy = 4.49993e-08 + model1: + number of parcels added = 17737 + mass introduced = 1.47498e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.129, 532.24 + Mass transfer phase change = 5.22823e-11 + D10, D32, Dmax (mu) = 52.7932, 83.9803, 150.439 + Liquid penetration 95% mass (m) = 0.00737763 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00760372, Final residual = 3.46897e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0151573, Final residual = 4.88274e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00175221, Final residual = 1.33903e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00297664, Final residual = 2.21017e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00349461, Final residual = 2.84467e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00349459, Final residual = 2.84755e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00233854, Final residual = 1.15778e-07, No Iterations 1 +min/max(T) = 622.916, 1271.12 +GAMG: Solving for p, Initial residual = 0.0484256, Final residual = 5.66027e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.07718e-06, global = 3.01042e-06, cumulative = 0.00120301 +GAMG: Solving for p, Initial residual = 5.30911e-05, Final residual = 6.15384e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.01584e-06, global = 3.01518e-06, cumulative = 0.00120602 +smoothSolver: Solving for epsilon, Initial residual = 0.000967988, Final residual = 1.40949e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00201301, Final residual = 3.61593e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.074312 s +other Time = 1e-06 s +rho Equations = 0.000201 s +U Equations = 0.001243 s +Y Equations = 0.00223399 s +E Equations = 0.000502 s +p Equations = 0.002158 s +calculate parcels = 52.2035 s +chemistry correctThermo = 0.00237 s +turbulence correct = 0.000983 s +combustion correct(in Y) = 0.064392 s +percentage of chemistry = 86.6509 % +percentage of rho/U/Y/E = 5.62492 % +========Time details of each equation======= +rhoEqn Time = 0.000357 s +rhoEqn assamble = 0.000282 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001243 s +UEqn assamble = 0.00073 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000513 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001561 s +YEqn assamble = 0.000573 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 7.8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000377 s +EEqn assamble = 0.000285 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 88.46 s ClockTime = 89 s +Courant Number mean: 0.00221816 max: 0.0174249 +Time = 0.001005 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 17766 + Current mass in system = 1.42477e-09 + Linear momentum = (2.81181e-11 -1.10555e-08 0) + |Linear momentum| = 1.10555e-08 + Linear kinetic energy = 4.49765e-08 + model1: + number of parcels added = 17786 + mass introduced = 1.47732e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.146, 532.406 + Mass transfer phase change = 5.25441e-11 + D10, D32, Dmax (mu) = 52.5934, 83.9904, 150.448 + Liquid penetration 95% mass (m) = 0.00739387 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00756817, Final residual = 3.4741e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0152307, Final residual = 4.93108e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00174687, Final residual = 1.32866e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00299354, Final residual = 2.2434e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00351331, Final residual = 2.88396e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00351329, Final residual = 2.88699e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00235216, Final residual = 1.16241e-07, No Iterations 1 +min/max(T) = 622.92, 1282.95 +GAMG: Solving for p, Initial residual = 0.0482315, Final residual = 6.51502e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.09353e-06, global = 3.01237e-06, cumulative = 0.00120903 +GAMG: Solving for p, Initial residual = 6.06714e-05, Final residual = 6.21833e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.01837e-06, global = 3.01764e-06, cumulative = 0.00121205 +smoothSolver: Solving for epsilon, Initial residual = 0.000971888, Final residual = 1.41945e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00201563, Final residual = 3.63108e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.079196 s +other Time = 1e-06 s +rho Equations = 0.000165 s +U Equations = 0.00105 s +Y Equations = 0.00241459 s +E Equations = 0.000594 s +p Equations = 0.002612 s +calculate parcels = 52.4238 s +chemistry correctThermo = 0.002795 s +turbulence correct = 0.001191 s +combustion correct(in Y) = 0.0681574 s +percentage of chemistry = 86.0617 % +percentage of rho/U/Y/E = 5.33308 % +========Time details of each equation======= +rhoEqn Time = 0.000354 s +rhoEqn assamble = 0.000281 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001049 s +UEqn assamble = 0.000606 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000443 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00183 s +YEqn assamble = 0.000657 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000208 s +YEqn correct boundary = 0 s +EEqn Time = 0.000441 s +EEqn assamble = 0.00033 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 88.76 s ClockTime = 89 s +Courant Number mean: 0.00225854 max: 0.0174391 +Time = 0.0010075 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 17814 + Current mass in system = 1.42679e-09 + Linear momentum = (2.85673e-11 -1.10608e-08 0) + |Linear momentum| = 1.10609e-08 + Linear kinetic energy = 4.49523e-08 + model1: + number of parcels added = 17834 + mass introduced = 1.47959e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.128, 532.532 + Mass transfer phase change = 5.28061e-11 + D10, D32, Dmax (mu) = 52.6044, 84.0222, 150.456 + Liquid penetration 95% mass (m) = 0.00740799 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00774735, Final residual = 3.59127e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0153124, Final residual = 4.98803e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00174933, Final residual = 1.33085e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00301286, Final residual = 2.276e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00353535, Final residual = 2.92418e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00353533, Final residual = 2.92723e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00236414, Final residual = 1.16944e-07, No Iterations 1 +min/max(T) = 622.951, 1295.05 +GAMG: Solving for p, Initial residual = 0.048108, Final residual = 6.9148e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.1132e-06, global = 3.01413e-06, cumulative = 0.00121507 +GAMG: Solving for p, Initial residual = 6.25577e-05, Final residual = 6.1952e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.02107e-06, global = 3.02022e-06, cumulative = 0.00121809 +smoothSolver: Solving for epsilon, Initial residual = 0.000976278, Final residual = 1.4303e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0020191, Final residual = 3.64861e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094159 s +other Time = 0 s +rho Equations = 0.00017 s +U Equations = 0.001161 s +Y Equations = 0.00242049 s +E Equations = 0.000619 s +p Equations = 0.002117 s +calculate parcels = 52.6967 s +chemistry correctThermo = 0.002846 s +turbulence correct = 0.001054 s +combustion correct(in Y) = 0.0835675 s +percentage of chemistry = 88.7515 % +percentage of rho/U/Y/E = 4.64161 % +========Time details of each equation======= +rhoEqn Time = 0.000312 s +rhoEqn assamble = 0.000245 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001159 s +UEqn assamble = 0.000667 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000492 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001786 s +YEqn assamble = 0.00065 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000202 s +YEqn correct boundary = 0 s +EEqn Time = 0.000466 s +EEqn assamble = 0.000347 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000119 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 89.13 s ClockTime = 90 s +Courant Number mean: 0.00229998 max: 0.0174586 +Time = 0.00101 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 17858 + Current mass in system = 1.4286e-09 + Linear momentum = (2.90575e-11 -1.10648e-08 0) + |Linear momentum| = 1.10648e-08 + Linear kinetic energy = 4.49231e-08 + model1: + number of parcels added = 17878 + mass introduced = 1.48167e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.125, 532.618 + Mass transfer phase change = 5.30684e-11 + D10, D32, Dmax (mu) = 52.5951, 84.04, 150.465 + Liquid penetration 95% mass (m) = 0.0074217 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00812624, Final residual = 3.74098e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0153868, Final residual = 5.04966e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0017564, Final residual = 1.3395e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00303345, Final residual = 2.30969e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00355896, Final residual = 2.96659e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00355895, Final residual = 2.96957e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0023772, Final residual = 1.18057e-07, No Iterations 1 +min/max(T) = 623, 1307.4 +GAMG: Solving for p, Initial residual = 0.0480131, Final residual = 8.12604e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.1356e-06, global = 3.01565e-06, cumulative = 0.0012211 +GAMG: Solving for p, Initial residual = 7.44842e-05, Final residual = 9.36512e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.02383e-06, global = 3.02253e-06, cumulative = 0.00122412 +smoothSolver: Solving for epsilon, Initial residual = 0.000981688, Final residual = 1.44378e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0020235, Final residual = 3.67205e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.101362 s +other Time = 1e-06 s +rho Equations = 0.000182 s +U Equations = 0.001205 s +Y Equations = 0.00240776 s +E Equations = 0.00061 s +p Equations = 0.002028 s +calculate parcels = 52.9778 s +chemistry correctThermo = 0.002795 s +turbulence correct = 0.000998 s +combustion correct(in Y) = 0.0909292 s +percentage of chemistry = 89.7074 % +percentage of rho/U/Y/E = 4.34558 % +========Time details of each equation======= +rhoEqn Time = 0.000326 s +rhoEqn assamble = 0.000256 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001204 s +UEqn assamble = 0.000695 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000509 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001759 s +YEqn assamble = 0.000645 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000182 s +YEqn correct boundary = 0 s +EEqn Time = 0.000455 s +EEqn assamble = 0.000341 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 89.51 s ClockTime = 90 s +Courant Number mean: 0.00234268 max: 0.0174798 +Time = 0.0010125 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 54 new parcels + +Cloud: sprayCloud + Current number of parcels = 17912 + Current mass in system = 1.43086e-09 + Linear momentum = (2.89064e-11 -1.10719e-08 0) + |Linear momentum| = 1.1072e-08 + Linear kinetic energy = 4.4906e-08 + model1: + number of parcels added = 17932 + mass introduced = 1.48419e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.139, 532.66 + Mass transfer phase change = 5.33307e-11 + D10, D32, Dmax (mu) = 52.5992, 84.0655, 150.474 + Liquid penetration 95% mass (m) = 0.00743659 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00863982, Final residual = 3.94587e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0154655, Final residual = 5.12201e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00176245, Final residual = 1.36173e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00305434, Final residual = 2.34406e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00358288, Final residual = 3.01078e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00358287, Final residual = 3.0138e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00239186, Final residual = 1.19363e-07, No Iterations 1 +min/max(T) = 623.075, 1319.98 +GAMG: Solving for p, Initial residual = 0.0479345, Final residual = 8.46718e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.14453e-06, global = 3.01557e-06, cumulative = 0.00122714 +GAMG: Solving for p, Initial residual = 7.74636e-05, Final residual = 7.5936e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.02484e-06, global = 3.02374e-06, cumulative = 0.00123016 +smoothSolver: Solving for epsilon, Initial residual = 0.000988062, Final residual = 1.45959e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00202903, Final residual = 3.69964e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.099964 s +other Time = 0 s +rho Equations = 0.000174 s +U Equations = 0.001263 s +Y Equations = 0.00241398 s +E Equations = 0.000614 s +p Equations = 0.002226 s +calculate parcels = 53.2896 s +chemistry correctThermo = 0.002919 s +turbulence correct = 0.001027 s +combustion correct(in Y) = 0.089104 s +percentage of chemistry = 89.1361 % +percentage of rho/U/Y/E = 4.46659 % +========Time details of each equation======= +rhoEqn Time = 0.000325 s +rhoEqn assamble = 0.000259 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001263 s +UEqn assamble = 0.000768 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000495 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001764 s +YEqn assamble = 0.000646 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000183 s +YEqn correct boundary = 0 s +EEqn Time = 0.000456 s +EEqn assamble = 0.00034 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 89.92 s ClockTime = 90 s +Courant Number mean: 0.00238677 max: 0.0174933 +Time = 0.001015 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 17963 + Current mass in system = 1.43297e-09 + Linear momentum = (2.90857e-11 -1.10781e-08 0) + |Linear momentum| = 1.10781e-08 + Linear kinetic energy = 4.48853e-08 + model1: + number of parcels added = 17983 + mass introduced = 1.48657e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.135, 532.661 + Mass transfer phase change = 5.35931e-11 + D10, D32, Dmax (mu) = 52.5791, 84.0825, 150.483 + Liquid penetration 95% mass (m) = 0.00745091 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00921602, Final residual = 4.23812e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0155532, Final residual = 5.20423e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00176817, Final residual = 1.38663e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00307499, Final residual = 2.37969e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00360616, Final residual = 3.05456e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00360615, Final residual = 3.05762e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00240984, Final residual = 1.20922e-07, No Iterations 1 +min/max(T) = 623.171, 1332.76 +GAMG: Solving for p, Initial residual = 0.0478485, Final residual = 8.1135e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.14329e-06, global = 3.01687e-06, cumulative = 0.00123318 +GAMG: Solving for p, Initial residual = 7.4525e-05, Final residual = 6.03191e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.02573e-06, global = 3.02483e-06, cumulative = 0.00123621 +smoothSolver: Solving for epsilon, Initial residual = 0.000995832, Final residual = 1.47712e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00203568, Final residual = 3.73049e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103176 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001159 s +Y Equations = 0.0023729 s +E Equations = 0.000605 s +p Equations = 0.002062 s +calculate parcels = 53.5826 s +chemistry correctThermo = 0.002798 s +turbulence correct = 0.000973 s +combustion correct(in Y) = 0.0928161 s +percentage of chemistry = 89.959 % +percentage of rho/U/Y/E = 4.18111 % +========Time details of each equation======= +rhoEqn Time = 0.000322 s +rhoEqn assamble = 0.000256 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001158 s +UEqn assamble = 0.000666 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000492 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001726 s +YEqn assamble = 0.000628 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000169 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000338 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 90.32 s ClockTime = 91 s +Courant Number mean: 0.00243223 max: 0.0174991 +Time = 0.0010175 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 18013 + Current mass in system = 1.43503e-09 + Linear momentum = (2.92379e-11 -1.10839e-08 0) + |Linear momentum| = 1.10839e-08 + Linear kinetic energy = 4.48635e-08 + model1: + number of parcels added = 18033 + mass introduced = 1.48889e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.137, 532.618 + Mass transfer phase change = 5.38556e-11 + D10, D32, Dmax (mu) = 52.5884, 84.1019, 150.492 + Liquid penetration 95% mass (m) = 0.00746722 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00975623, Final residual = 4.53263e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.015648, Final residual = 5.28886e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00177133, Final residual = 1.39726e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00309545, Final residual = 2.41607e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00362887, Final residual = 3.09727e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00362886, Final residual = 3.10037e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00242797, Final residual = 1.22293e-07, No Iterations 1 +min/max(T) = 623.281, 1345.68 +GAMG: Solving for p, Initial residual = 0.0477693, Final residual = 7.23784e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.1342e-06, global = 3.01757e-06, cumulative = 0.00123922 +GAMG: Solving for p, Initial residual = 6.67568e-05, Final residual = 4.43024e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.02625e-06, global = 3.02559e-06, cumulative = 0.00124225 +smoothSolver: Solving for epsilon, Initial residual = 0.00100526, Final residual = 1.49499e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00204257, Final residual = 3.76413e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102494 s +other Time = 0 s +rho Equations = 0.000151 s +U Equations = 0.001011 s +Y Equations = 0.00249983 s +E Equations = 0.000601 s +p Equations = 0.001667 s +calculate parcels = 53.8456 s +chemistry correctThermo = 0.002552 s +turbulence correct = 0.000893 s +combustion correct(in Y) = 0.0929312 s +percentage of chemistry = 90.6699 % +percentage of rho/U/Y/E = 4.1591 % +========Time details of each equation======= +rhoEqn Time = 0.000268 s +rhoEqn assamble = 0.000214 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00101 s +UEqn assamble = 0.000581 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000429 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001929 s +YEqn assamble = 0.000659 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000221 s +YEqn correct boundary = 0 s +EEqn Time = 0.000444 s +EEqn assamble = 0.00033 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 90.69 s ClockTime = 91 s +Courant Number mean: 0.00247902 max: 0.0175046 +Time = 0.00102 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 55 new parcels + +Cloud: sprayCloud + Current number of parcels = 18068 + Current mass in system = 1.43731e-09 + Linear momentum = (2.89136e-11 -1.10912e-08 0) + |Linear momentum| = 1.10913e-08 + Linear kinetic energy = 4.48477e-08 + model1: + number of parcels added = 18088 + mass introduced = 1.49143e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.135, 532.524 + Mass transfer phase change = 5.41183e-11 + D10, D32, Dmax (mu) = 52.5244, 84.1117, 150.501 + Liquid penetration 95% mass (m) = 0.0074817 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0101977, Final residual = 4.7975e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0157473, Final residual = 5.37273e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00177552, Final residual = 1.40179e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00311445, Final residual = 2.45026e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00364922, Final residual = 3.1383e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0036492, Final residual = 3.14144e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00244906, Final residual = 1.23877e-07, No Iterations 1 +min/max(T) = 623.415, 1358.71 +GAMG: Solving for p, Initial residual = 0.0476644, Final residual = 6.76318e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.12895e-06, global = 3.01883e-06, cumulative = 0.00124527 +GAMG: Solving for p, Initial residual = 6.27635e-05, Final residual = 5.52924e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.02757e-06, global = 3.02672e-06, cumulative = 0.00124829 +smoothSolver: Solving for epsilon, Initial residual = 0.00101528, Final residual = 1.5128e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00204959, Final residual = 3.80155e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.072531 s +other Time = 1e-06 s +rho Equations = 0.000185 s +U Equations = 0.001289 s +Y Equations = 0.00231543 s +E Equations = 0.00052 s +p Equations = 0.001909 s +calculate parcels = 54.1 s +chemistry correctThermo = 0.001971 s +turbulence correct = 0.000837 s +combustion correct(in Y) = 0.0633186 s +percentage of chemistry = 87.2986 % +percentage of rho/U/Y/E = 5.9415 % +========Time details of each equation======= +rhoEqn Time = 0.000317 s +rhoEqn assamble = 0.000243 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001289 s +UEqn assamble = 0.000835 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000454 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001635 s +YEqn assamble = 0.000586 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000135 s +YEqn correct boundary = 0 s +EEqn Time = 0.000388 s +EEqn assamble = 0.00029 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 91.01 s ClockTime = 91 s +Courant Number mean: 0.0025271 max: 0.0175354 +Time = 0.0010225 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 53 new parcels + +Cloud: sprayCloud + Current number of parcels = 18121 + Current mass in system = 1.43949e-09 + Linear momentum = (2.92141e-11 -1.10979e-08 0) + |Linear momentum| = 1.1098e-08 + Linear kinetic energy = 4.48298e-08 + model1: + number of parcels added = 18141 + mass introduced = 1.49387e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.14, 532.723 + Mass transfer phase change = 5.43809e-11 + D10, D32, Dmax (mu) = 52.5318, 84.134, 150.51 + Liquid penetration 95% mass (m) = 0.00749785 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.010366, Final residual = 5.01542e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0158571, Final residual = 5.45541e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0017771, Final residual = 1.42195e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0031302, Final residual = 2.48236e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00366512, Final residual = 3.17301e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0036651, Final residual = 3.17617e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00247107, Final residual = 1.25488e-07, No Iterations 1 +min/max(T) = 623.574, 1371.77 +GAMG: Solving for p, Initial residual = 0.0475714, Final residual = 7.47179e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.13782e-06, global = 3.01862e-06, cumulative = 0.00125131 +GAMG: Solving for p, Initial residual = 7.1304e-05, Final residual = 6.57082e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.02803e-06, global = 3.02696e-06, cumulative = 0.00125434 +smoothSolver: Solving for epsilon, Initial residual = 0.00102581, Final residual = 1.53135e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0020568, Final residual = 3.84264e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.098791 s +other Time = 1e-06 s +rho Equations = 0.00017 s +U Equations = 0.001208 s +Y Equations = 0.00216199 s +E Equations = 0.000517 s +p Equations = 0.002077 s +calculate parcels = 54.3633 s +chemistry correctThermo = 0.002081 s +turbulence correct = 0.001003 s +combustion correct(in Y) = 0.08937 s +percentage of chemistry = 90.4637 % +percentage of rho/U/Y/E = 4.10664 % +========Time details of each equation======= +rhoEqn Time = 0.000329 s +rhoEqn assamble = 0.00025 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001208 s +UEqn assamble = 0.000677 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000531 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001499 s +YEqn assamble = 0.000558 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000114 s +YEqn correct boundary = 0 s +EEqn Time = 0.000393 s +EEqn assamble = 0.000297 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 91.38 s ClockTime = 92 s +Courant Number mean: 0.00257618 max: 0.0175687 +Time = 0.001025 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 18171 + Current mass in system = 1.44152e-09 + Linear momentum = (2.96956e-11 -1.11036e-08 0) + |Linear momentum| = 1.11037e-08 + Linear kinetic energy = 4.48086e-08 + model1: + number of parcels added = 18191 + mass introduced = 1.49616e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.144, 533.028 + Mass transfer phase change = 5.46435e-11 + D10, D32, Dmax (mu) = 52.5282, 84.145, 150.52 + Liquid penetration 95% mass (m) = 0.00751206 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0102896, Final residual = 5.14123e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0159502, Final residual = 5.52043e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00179406, Final residual = 1.44554e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00314875, Final residual = 2.51344e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00368471, Final residual = 3.21131e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00368469, Final residual = 3.2145e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00249544, Final residual = 1.27992e-07, No Iterations 1 +min/max(T) = 623.754, 1384.79 +GAMG: Solving for p, Initial residual = 0.0473883, Final residual = 8.15344e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.13903e-06, global = 3.01861e-06, cumulative = 0.00125736 +GAMG: Solving for p, Initial residual = 7.86715e-05, Final residual = 6.12751e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.02773e-06, global = 3.02695e-06, cumulative = 0.00126039 +smoothSolver: Solving for epsilon, Initial residual = 0.00103536, Final residual = 1.54848e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00206304, Final residual = 3.88428e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.072893 s +other Time = 0 s +rho Equations = 0.000178 s +U Equations = 0.001202 s +Y Equations = 0.00206362 s +E Equations = 0.000495 s +p Equations = 0.001754 s +calculate parcels = 54.6458 s +chemistry correctThermo = 0.002038 s +turbulence correct = 0.000843 s +combustion correct(in Y) = 0.0641184 s +percentage of chemistry = 87.9623 % +percentage of rho/U/Y/E = 5.40328 % +========Time details of each equation======= +rhoEqn Time = 0.0003 s +rhoEqn assamble = 0.000237 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001201 s +UEqn assamble = 0.000703 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000498 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001418 s +YEqn assamble = 0.000534 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.1e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000372 s +EEqn assamble = 0.000279 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 91.73 s ClockTime = 92 s +Courant Number mean: 0.00262609 max: 0.0175997 +Time = 0.0010275 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 18222 + Current mass in system = 1.44358e-09 + Linear momentum = (3.00122e-11 -1.11096e-08 0) + |Linear momentum| = 1.11096e-08 + Linear kinetic energy = 4.47887e-08 + model1: + number of parcels added = 18242 + mass introduced = 1.49849e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.131, 533.299 + Mass transfer phase change = 5.49062e-11 + D10, D32, Dmax (mu) = 52.538, 84.1837, 150.529 + Liquid penetration 95% mass (m) = 0.00752794 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00994216, Final residual = 5.08699e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0160254, Final residual = 5.58274e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0017989, Final residual = 1.45565e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00316651, Final residual = 2.5492e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00370322, Final residual = 3.25514e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00370321, Final residual = 3.25849e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00251625, Final residual = 1.29869e-07, No Iterations 1 +min/max(T) = 623.95, 1397.73 +GAMG: Solving for p, Initial residual = 0.0473288, Final residual = 9.35109e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.16133e-06, global = 3.01777e-06, cumulative = 0.0012634 +GAMG: Solving for p, Initial residual = 8.86636e-05, Final residual = 2.076e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.0276e-06, global = 3.02735e-06, cumulative = 0.00126643 +smoothSolver: Solving for epsilon, Initial residual = 0.00104443, Final residual = 1.56459e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00206885, Final residual = 3.92475e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.105893 s +other Time = 0 s +rho Equations = 0.000249 s +U Equations = 0.001472 s +Y Equations = 0.00250018 s +E Equations = 0.000603 s +p Equations = 0.002246 s +calculate parcels = 54.9312 s +chemistry correctThermo = 0.002801 s +turbulence correct = 0.00097 s +combustion correct(in Y) = 0.0948008 s +percentage of chemistry = 89.5251 % +percentage of rho/U/Y/E = 4.55572 % +========Time details of each equation======= +rhoEqn Time = 0.000393 s +rhoEqn assamble = 0.000311 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00147 s +UEqn assamble = 0.000873 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000597 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001696 s +YEqn assamble = 0.000656 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.7e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000447 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 92.12 s ClockTime = 93 s +Courant Number mean: 0.00267675 max: 0.0176364 +Time = 0.00103 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 64 new parcels + +Cloud: sprayCloud + Current number of parcels = 18286 + Current mass in system = 1.44623e-09 + Linear momentum = (2.99238e-11 -1.11196e-08 0) + |Linear momentum| = 1.11196e-08 + Linear kinetic energy = 4.47831e-08 + model1: + number of parcels added = 18306 + mass introduced = 1.5014e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.129, 533.532 + Mass transfer phase change = 5.5169e-11 + D10, D32, Dmax (mu) = 52.5287, 84.2025, 150.539 + Liquid penetration 95% mass (m) = 0.00754389 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00953557, Final residual = 4.91963e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.016105, Final residual = 5.64738e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0018048, Final residual = 1.47304e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00318729, Final residual = 2.58852e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00372544, Final residual = 3.30329e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00372543, Final residual = 3.30681e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00253756, Final residual = 1.31745e-07, No Iterations 1 +min/max(T) = 624.17, 1410.58 +GAMG: Solving for p, Initial residual = 0.0471981, Final residual = 8.9284e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.16497e-06, global = 3.02084e-06, cumulative = 0.00126945 +GAMG: Solving for p, Initial residual = 8.34721e-05, Final residual = 8.1691e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.03136e-06, global = 3.02999e-06, cumulative = 0.00127248 +smoothSolver: Solving for epsilon, Initial residual = 0.00105258, Final residual = 1.58002e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00207409, Final residual = 3.9641e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102568 s +other Time = 1e-06 s +rho Equations = 0.000174 s +U Equations = 0.001253 s +Y Equations = 0.00246542 s +E Equations = 0.000613 s +p Equations = 0.002155 s +calculate parcels = 55.2114 s +chemistry correctThermo = 0.002837 s +turbulence correct = 0.001108 s +combustion correct(in Y) = 0.0917426 s +percentage of chemistry = 89.4456 % +percentage of rho/U/Y/E = 4.39261 % +========Time details of each equation======= +rhoEqn Time = 0.000334 s +rhoEqn assamble = 0.000268 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001253 s +UEqn assamble = 0.000759 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000494 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001809 s +YEqn assamble = 0.000673 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000171 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000339 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 92.51 s ClockTime = 93 s +Courant Number mean: 0.00272826 max: 0.0176647 +Time = 0.0010325 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 52 new parcels + +Cloud: sprayCloud + Current number of parcels = 18338 + Current mass in system = 1.44833e-09 + Linear momentum = (2.99113e-11 -1.11259e-08 0) + |Linear momentum| = 1.11259e-08 + Linear kinetic energy = 4.47649e-08 + model1: + number of parcels added = 18358 + mass introduced = 1.50376e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.12, 533.731 + Mass transfer phase change = 5.54323e-11 + D10, D32, Dmax (mu) = 52.5277, 84.2189, 150.548 + Liquid penetration 95% mass (m) = 0.00755961 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00916253, Final residual = 4.81777e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0161893, Final residual = 5.72171e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00181229, Final residual = 1.48623e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00321037, Final residual = 2.63042e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0037505, Final residual = 3.35436e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00375049, Final residual = 3.35792e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00255538, Final residual = 1.33686e-07, No Iterations 1 +min/max(T) = 624.409, 1423.26 +GAMG: Solving for p, Initial residual = 0.0471657, Final residual = 8.38634e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.1645e-06, global = 3.02461e-06, cumulative = 0.00127551 +GAMG: Solving for p, Initial residual = 7.73403e-05, Final residual = 1.62873e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.03405e-06, global = 3.03378e-06, cumulative = 0.00127854 +smoothSolver: Solving for epsilon, Initial residual = 0.00105966, Final residual = 1.59598e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00207884, Final residual = 4.00543e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097454 s +other Time = 1e-06 s +rho Equations = 0.000287 s +U Equations = 0.001819 s +Y Equations = 0.00273451 s +E Equations = 0.000595 s +p Equations = 0.002188 s +calculate parcels = 55.5038 s +chemistry correctThermo = 0.002795 s +turbulence correct = 0.001039 s +combustion correct(in Y) = 0.0857235 s +percentage of chemistry = 87.963 % +percentage of rho/U/Y/E = 5.57751 % +========Time details of each equation======= +rhoEqn Time = 0.000424 s +rhoEqn assamble = 0.000327 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001817 s +UEqn assamble = 0.000946 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000871 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001623 s +YEqn assamble = 0.000737 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -6.3e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000442 s +EEqn assamble = 0.00033 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 92.9 s ClockTime = 93 s +Courant Number mean: 0.00278078 max: 0.0177023 +Time = 0.001035 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 18387 + Current mass in system = 1.45029e-09 + Linear momentum = (2.97447e-11 -1.11312e-08 0) + |Linear momentum| = 1.11312e-08 + Linear kinetic energy = 4.47436e-08 + model1: + number of parcels added = 18407 + mass introduced = 1.50598e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.14, 533.901 + Mass transfer phase change = 5.56959e-11 + D10, D32, Dmax (mu) = 52.5225, 84.2434, 150.558 + Liquid penetration 95% mass (m) = 0.00757459 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00891261, Final residual = 4.78486e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0162722, Final residual = 5.80712e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00182176, Final residual = 1.50322e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00323361, Final residual = 2.67098e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00377548, Final residual = 3.40481e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00377547, Final residual = 3.40841e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0025739, Final residual = 1.35759e-07, No Iterations 1 +min/max(T) = 624.673, 1435.69 +GAMG: Solving for p, Initial residual = 0.0471398, Final residual = 7.22584e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.16119e-06, global = 3.02967e-06, cumulative = 0.00128157 +GAMG: Solving for p, Initial residual = 6.583e-05, Final residual = 1.7195e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.03889e-06, global = 3.0386e-06, cumulative = 0.00128461 +smoothSolver: Solving for epsilon, Initial residual = 0.00106695, Final residual = 1.61655e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00208424, Final residual = 4.05191e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.082539 s +other Time = 0 s +rho Equations = 0.000205 s +U Equations = 0.001346 s +Y Equations = 0.00225123 s +E Equations = 0.000559 s +p Equations = 0.001901 s +calculate parcels = 55.8057 s +chemistry correctThermo = 0.002014 s +turbulence correct = 0.000933 s +combustion correct(in Y) = 0.0731128 s +percentage of chemistry = 88.5797 % +percentage of rho/U/Y/E = 5.28384 % +========Time details of each equation======= +rhoEqn Time = 0.000346 s +rhoEqn assamble = 0.000279 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001346 s +UEqn assamble = 0.000832 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000514 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001567 s +YEqn assamble = 0.000549 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000113 s +YEqn correct boundary = 0 s +EEqn Time = 0.000402 s +EEqn assamble = 0.000304 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 93.28 s ClockTime = 94 s +Courant Number mean: 0.00283436 max: 0.017741 +Time = 0.0010375 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 18433 + Current mass in system = 1.4521e-09 + Linear momentum = (2.96764e-11 -1.11356e-08 0) + |Linear momentum| = 1.11356e-08 + Linear kinetic energy = 4.47194e-08 + model1: + number of parcels added = 18453 + mass introduced = 1.50806e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.133, 534.041 + Mass transfer phase change = 5.596e-11 + D10, D32, Dmax (mu) = 52.5267, 84.2702, 150.568 + Liquid penetration 95% mass (m) = 0.00758965 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00884035, Final residual = 4.84177e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.016353, Final residual = 5.89827e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00183077, Final residual = 1.52211e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00325674, Final residual = 2.71237e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00379995, Final residual = 3.4559e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00379994, Final residual = 3.45959e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00259362, Final residual = 1.37882e-07, No Iterations 1 +min/max(T) = 624.967, 1447.78 +GAMG: Solving for p, Initial residual = 0.0471257, Final residual = 7.13113e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.16902e-06, global = 3.03536e-06, cumulative = 0.00128764 +GAMG: Solving for p, Initial residual = 6.46795e-05, Final residual = 7.89034e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.04567e-06, global = 3.04429e-06, cumulative = 0.00129069 +smoothSolver: Solving for epsilon, Initial residual = 0.00107509, Final residual = 1.63973e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00209063, Final residual = 4.10189e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.080569 s +other Time = 1e-06 s +rho Equations = 0.000174 s +U Equations = 0.00105 s +Y Equations = 0.00239172 s +E Equations = 0.000639 s +p Equations = 0.00211 s +calculate parcels = 56.0313 s +chemistry correctThermo = 0.002808 s +turbulence correct = 0.000992 s +combustion correct(in Y) = 0.0701873 s +percentage of chemistry = 87.1145 % +percentage of rho/U/Y/E = 5.28084 % +========Time details of each equation======= +rhoEqn Time = 0.000319 s +rhoEqn assamble = 0.000249 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001049 s +UEqn assamble = 0.000629 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00042 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001818 s +YEqn assamble = 0.000641 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000229 s +YEqn correct boundary = 0 s +EEqn Time = 0.000484 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000149 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 93.59 s ClockTime = 94 s +Courant Number mean: 0.0028892 max: 0.0177838 +Time = 0.00104 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 53 new parcels + +Cloud: sprayCloud + Current number of parcels = 18486 + Current mass in system = 1.4542e-09 + Linear momentum = (2.99372e-11 -1.1142e-08 0) + |Linear momentum| = 1.1142e-08 + Linear kinetic energy = 4.47026e-08 + model1: + number of parcels added = 18506 + mass introduced = 1.51043e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.136, 534.156 + Mass transfer phase change = 5.62247e-11 + D10, D32, Dmax (mu) = 52.5283, 84.2917, 150.578 + Liquid penetration 95% mass (m) = 0.00760497 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00896345, Final residual = 4.99974e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0164202, Final residual = 5.99052e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0018406, Final residual = 1.54388e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00327916, Final residual = 2.75316e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00382305, Final residual = 3.50545e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00382304, Final residual = 3.50916e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00261416, Final residual = 1.40069e-07, No Iterations 1 +min/max(T) = 625.286, 1459.43 +GAMG: Solving for p, Initial residual = 0.047092, Final residual = 7.32698e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.18125e-06, global = 3.04146e-06, cumulative = 0.00129373 +GAMG: Solving for p, Initial residual = 6.72278e-05, Final residual = 5.69608e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.05194e-06, global = 3.05095e-06, cumulative = 0.00129678 +smoothSolver: Solving for epsilon, Initial residual = 0.00108332, Final residual = 1.66295e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00209716, Final residual = 4.15343e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100677 s +other Time = 0 s +rho Equations = 0.000176 s +U Equations = 0.001185 s +Y Equations = 0.00246308 s +E Equations = 0.000615 s +p Equations = 0.002063 s +calculate parcels = 56.3373 s +chemistry correctThermo = 0.002807 s +turbulence correct = 0.000972 s +combustion correct(in Y) = 0.0901909 s +percentage of chemistry = 89.5844 % +percentage of rho/U/Y/E = 4.40923 % +========Time details of each equation======= +rhoEqn Time = 0.000325 s +rhoEqn assamble = 0.000258 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001185 s +UEqn assamble = 0.000681 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000504 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00184 s +YEqn assamble = 0.000654 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000192 s +YEqn correct boundary = 0 s +EEqn Time = 0.000457 s +EEqn assamble = 0.000343 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 93.99 s ClockTime = 94 s +Courant Number mean: 0.00294549 max: 0.017832 +Time = 0.0010425 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 18535 + Current mass in system = 1.45617e-09 + Linear momentum = (2.98933e-11 -1.11475e-08 0) + |Linear momentum| = 1.11476e-08 + Linear kinetic energy = 4.46831e-08 + model1: + number of parcels added = 18556 + mass introduced = 1.51266e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.122, 534.877 + Mass transfer phase change = 5.6491e-11 + D10, D32, Dmax (mu) = 52.7853, 84.3294, 150.588 + Liquid penetration 95% mass (m) = 0.00762025 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00919729, Final residual = 5.18563e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0164803, Final residual = 6.0795e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00184268, Final residual = 1.55112e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00330146, Final residual = 2.80208e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0038442, Final residual = 3.5602e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00384419, Final residual = 3.56401e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00263484, Final residual = 1.42128e-07, No Iterations 1 +min/max(T) = 625.632, 1470.52 +GAMG: Solving for p, Initial residual = 0.0470395, Final residual = 6.82991e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.19173e-06, global = 3.06012e-06, cumulative = 0.00129984 +GAMG: Solving for p, Initial residual = 6.27215e-05, Final residual = 5.96245e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.07002e-06, global = 3.06902e-06, cumulative = 0.00130291 +smoothSolver: Solving for epsilon, Initial residual = 0.00109129, Final residual = 1.68834e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00210338, Final residual = 4.20537e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.091808 s +other Time = 0 s +rho Equations = 0.000151 s +U Equations = 0.000992 s +Y Equations = 0.00199861 s +E Equations = 0.00058 s +p Equations = 0.002103 s +calculate parcels = 56.6314 s +chemistry correctThermo = 0.002784 s +turbulence correct = 0.001152 s +combustion correct(in Y) = 0.0818194 s +percentage of chemistry = 89.1201 % +percentage of rho/U/Y/E = 4.05369 % +========Time details of each equation======= +rhoEqn Time = 0.0003 s +rhoEqn assamble = 0.000239 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00099 s +UEqn assamble = 0.000561 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000429 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001449 s +YEqn assamble = 0.000534 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000129 s +YEqn correct boundary = 0 s +EEqn Time = 0.000434 s +EEqn assamble = 0.000318 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 94.38 s ClockTime = 95 s +Courant Number mean: 0.00300322 max: 0.0178751 +Time = 0.001045 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 32 new parcels + +Cloud: sprayCloud + Current number of parcels = 18567 + Current mass in system = 1.45732e-09 + Linear momentum = (2.94863e-11 -1.11478e-08 0) + |Linear momentum| = 1.11478e-08 + Linear kinetic energy = 4.46461e-08 + model1: + number of parcels added = 18588 + mass introduced = 1.51408e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.128, 535.554 + Mass transfer phase change = 5.67568e-11 + D10, D32, Dmax (mu) = 52.7867, 84.3515, 150.597 + Liquid penetration 95% mass (m) = 0.00763642 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00946843, Final residual = 5.41891e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0165417, Final residual = 6.16612e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00185648, Final residual = 1.59698e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0033198, Final residual = 2.85068e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00386295, Final residual = 3.61876e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00386294, Final residual = 3.62262e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00266014, Final residual = 1.45186e-07, No Iterations 1 +min/max(T) = 626.003, 1480.95 +GAMG: Solving for p, Initial residual = 0.0469807, Final residual = 6.26211e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.177e-06, global = 3.05537e-06, cumulative = 0.00130596 +GAMG: Solving for p, Initial residual = 5.82702e-05, Final residual = 4.94802e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.06517e-06, global = 3.06426e-06, cumulative = 0.00130903 +smoothSolver: Solving for epsilon, Initial residual = 0.0010991, Final residual = 1.71553e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00210915, Final residual = 4.25627e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102746 s +other Time = 0 s +rho Equations = 0.000208 s +U Equations = 0.001308 s +Y Equations = 0.00238137 s +E Equations = 0.000591 s +p Equations = 0.002091 s +calculate parcels = 56.9442 s +chemistry correctThermo = 0.002789 s +turbulence correct = 0.001012 s +combustion correct(in Y) = 0.0921206 s +percentage of chemistry = 89.6586 % +percentage of rho/U/Y/E = 4.36841 % +========Time details of each equation======= +rhoEqn Time = 0.000352 s +rhoEqn assamble = 0.000283 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001306 s +UEqn assamble = 0.000795 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000511 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001737 s +YEqn assamble = 0.000646 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000168 s +YEqn correct boundary = 0 s +EEqn Time = 0.000436 s +EEqn assamble = 0.000324 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 94.8 s ClockTime = 95 s +Courant Number mean: 0.00306231 max: 0.0179041 +Time = 0.0010475 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 18618 + Current mass in system = 1.45931e-09 + Linear momentum = (2.96555e-11 -1.11536e-08 0) + |Linear momentum| = 1.11537e-08 + Linear kinetic energy = 4.46289e-08 + model1: + number of parcels added = 18639 + mass introduced = 1.51633e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.16, 536.183 + Mass transfer phase change = 5.70235e-11 + D10, D32, Dmax (mu) = 52.7845, 84.3628, 150.607 + Liquid penetration 95% mass (m) = 0.00765197 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00965727, Final residual = 5.63198e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0166037, Final residual = 6.25032e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0018689, Final residual = 1.64016e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0033385, Final residual = 2.90458e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00388006, Final residual = 3.68015e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00388006, Final residual = 3.68407e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00268839, Final residual = 1.48346e-07, No Iterations 1 +min/max(T) = 626.407, 1490.6 +GAMG: Solving for p, Initial residual = 0.0468928, Final residual = 5.90619e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.17934e-06, global = 3.06499e-06, cumulative = 0.00131209 +GAMG: Solving for p, Initial residual = 5.50986e-05, Final residual = 4.50513e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.07478e-06, global = 3.07395e-06, cumulative = 0.00131517 +smoothSolver: Solving for epsilon, Initial residual = 0.00110773, Final residual = 1.74414e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00211605, Final residual = 4.31114e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.08511 s +other Time = 0 s +rho Equations = 0.000196 s +U Equations = 0.001276 s +Y Equations = 0.00204005 s +E Equations = 0.000482 s +p Equations = 0.001743 s +calculate parcels = 57.256 s +chemistry correctThermo = 0.002 s +turbulence correct = 0.0008 s +combustion correct(in Y) = 0.076378 s +percentage of chemistry = 89.7403 % +percentage of rho/U/Y/E = 4.69281 % +========Time details of each equation======= +rhoEqn Time = 0.000322 s +rhoEqn assamble = 0.000238 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001276 s +UEqn assamble = 0.000779 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000497 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001385 s +YEqn assamble = 0.000516 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000367 s +EEqn assamble = 0.000274 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 95.19 s ClockTime = 96 s +Courant Number mean: 0.0031228 max: 0.0179387 +Time = 0.00105 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 18669 + Current mass in system = 1.46128e-09 + Linear momentum = (2.97441e-11 -1.11596e-08 0) + |Linear momentum| = 1.11596e-08 + Linear kinetic energy = 4.46124e-08 + model1: + number of parcels added = 18690 + mass introduced = 1.51858e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.131, 536.763 + Mass transfer phase change = 5.72911e-11 + D10, D32, Dmax (mu) = 52.7813, 84.3877, 150.617 + Liquid penetration 95% mass (m) = 0.00766743 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00969053, Final residual = 5.81439e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0166558, Final residual = 6.32845e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0018811, Final residual = 1.67434e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00335534, Final residual = 2.95775e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00389467, Final residual = 3.74419e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00389467, Final residual = 3.74817e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0027168, Final residual = 1.51298e-07, No Iterations 1 +min/max(T) = 626.841, 1499.39 +GAMG: Solving for p, Initial residual = 0.0467878, Final residual = 6.40857e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.19878e-06, global = 3.07459e-06, cumulative = 0.00131824 +GAMG: Solving for p, Initial residual = 6.05755e-05, Final residual = 4.6016e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.08464e-06, global = 3.0838e-06, cumulative = 0.00132133 +smoothSolver: Solving for epsilon, Initial residual = 0.00111602, Final residual = 1.77456e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00212387, Final residual = 4.36729e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.099443 s +other Time = 1e-06 s +rho Equations = 0.000182 s +U Equations = 0.001306 s +Y Equations = 0.00241704 s +E Equations = 0.000621 s +p Equations = 0.002262 s +calculate parcels = 57.5531 s +chemistry correctThermo = 0.002804 s +turbulence correct = 0.001112 s +combustion correct(in Y) = 0.088513 s +percentage of chemistry = 89.0087 % +percentage of rho/U/Y/E = 4.5514 % +========Time details of each equation======= +rhoEqn Time = 0.000342 s +rhoEqn assamble = 0.000272 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001305 s +UEqn assamble = 0.000803 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000502 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001782 s +YEqn assamble = 0.000644 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000171 s +YEqn correct boundary = 0 s +EEqn Time = 0.000465 s +EEqn assamble = 0.000339 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000126 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 95.59 s ClockTime = 96 s +Courant Number mean: 0.00318434 max: 0.0179691 +Time = 0.0010525 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 18713 + Current mass in system = 1.46295e-09 + Linear momentum = (2.97889e-11 -1.11636e-08 0) + |Linear momentum| = 1.11636e-08 + Linear kinetic energy = 4.45899e-08 + model1: + number of parcels added = 18734 + mass introduced = 1.52051e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.125, 537.291 + Mass transfer phase change = 5.75597e-11 + D10, D32, Dmax (mu) = 52.7825, 84.4151, 150.626 + Liquid penetration 95% mass (m) = 0.00768423 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00955513, Final residual = 5.91882e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0166953, Final residual = 6.395e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00189252, Final residual = 1.70377e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00337013, Final residual = 3.0182e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00390623, Final residual = 3.80855e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00390623, Final residual = 3.8127e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0027444, Final residual = 1.54181e-07, No Iterations 1 +min/max(T) = 627.297, 1507.24 +GAMG: Solving for p, Initial residual = 0.0466594, Final residual = 6.7838e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.22092e-06, global = 3.0853e-06, cumulative = 0.00132441 +GAMG: Solving for p, Initial residual = 6.59934e-05, Final residual = 5.00249e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.09644e-06, global = 3.09546e-06, cumulative = 0.00132751 +smoothSolver: Solving for epsilon, Initial residual = 0.00112362, Final residual = 1.80435e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00213215, Final residual = 4.42172e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.071236 s +other Time = 1e-06 s +rho Equations = 0.000191 s +U Equations = 0.001155 s +Y Equations = 0.00227399 s +E Equations = 0.000508 s +p Equations = 0.001772 s +calculate parcels = 57.8076 s +chemistry correctThermo = 0.001926 s +turbulence correct = 0.000868 s +combustion correct(in Y) = 0.062354 s +percentage of chemistry = 87.5316 % +percentage of rho/U/Y/E = 5.7948 % +========Time details of each equation======= +rhoEqn Time = 0.000319 s +rhoEqn assamble = 0.000258 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001152 s +UEqn assamble = 0.000607 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000545 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001671 s +YEqn assamble = 0.000567 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000122 s +YEqn correct boundary = 0 s +EEqn Time = 0.000382 s +EEqn assamble = 0.000288 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 95.91 s ClockTime = 96 s +Courant Number mean: 0.00324676 max: 0.0180007 +Time = 0.001055 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 41 new parcels + +Cloud: sprayCloud + Current number of parcels = 18754 + Current mass in system = 1.46448e-09 + Linear momentum = (2.96821e-11 -1.11667e-08 0) + |Linear momentum| = 1.11668e-08 + Linear kinetic energy = 4.4565e-08 + model1: + number of parcels added = 18775 + mass introduced = 1.52231e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.125, 537.766 + Mass transfer phase change = 5.78294e-11 + D10, D32, Dmax (mu) = 52.7569, 84.4295, 150.636 + Liquid penetration 95% mass (m) = 0.00769998 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00923406, Final residual = 5.90519e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0167125, Final residual = 6.44761e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00190213, Final residual = 1.73647e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00338363, Final residual = 3.07763e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00391583, Final residual = 3.87743e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00391583, Final residual = 3.88164e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00277242, Final residual = 1.57069e-07, No Iterations 1 +min/max(T) = 627.771, 1514.13 +GAMG: Solving for p, Initial residual = 0.0465074, Final residual = 7.12276e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.23814e-06, global = 3.09818e-06, cumulative = 0.00133061 +GAMG: Solving for p, Initial residual = 6.95382e-05, Final residual = 5.16588e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.11036e-06, global = 3.10933e-06, cumulative = 0.00133371 +smoothSolver: Solving for epsilon, Initial residual = 0.00113038, Final residual = 1.83266e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00213956, Final residual = 4.47322e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.110357 s +other Time = 0 s +rho Equations = 0.000269 s +U Equations = 0.001351 s +Y Equations = 0.00300254 s +E Equations = 0.000733 s +p Equations = 0.003031 s +calculate parcels = 58.109 s +chemistry correctThermo = 0.002841 s +turbulence correct = 0.001398 s +combustion correct(in Y) = 0.0974685 s +percentage of chemistry = 88.3211 % +percentage of rho/U/Y/E = 4.85292 % +========Time details of each equation======= +rhoEqn Time = 0.000516 s +rhoEqn assamble = 0.000403 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000113 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001351 s +UEqn assamble = 0.000821 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00053 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002291 s +YEqn assamble = 0.000781 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000192 s +YEqn correct boundary = 0 s +EEqn Time = 0.000553 s +EEqn assamble = 0.000414 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000139 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 96.33 s ClockTime = 97 s +Courant Number mean: 0.00330988 max: 0.0180289 +Time = 0.0010575 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 18803 + Current mass in system = 1.46634e-09 + Linear momentum = (2.99995e-11 -1.11722e-08 0) + |Linear momentum| = 1.11723e-08 + Linear kinetic energy = 4.45485e-08 + model1: + number of parcels added = 18824 + mass introduced = 1.52444e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.134, 538.189 + Mass transfer phase change = 5.81005e-11 + D10, D32, Dmax (mu) = 52.7642, 84.4534, 150.645 + Liquid penetration 95% mass (m) = 0.00771622 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00873682, Final residual = 5.77586e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0167106, Final residual = 6.48746e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00191262, Final residual = 1.76928e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00339591, Final residual = 3.13269e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00392372, Final residual = 3.94404e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00392373, Final residual = 3.94852e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00279999, Final residual = 1.59918e-07, No Iterations 1 +min/max(T) = 628.267, 1520.12 +GAMG: Solving for p, Initial residual = 0.0463421, Final residual = 7.50337e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.2638e-06, global = 3.11255e-06, cumulative = 0.00133683 +GAMG: Solving for p, Initial residual = 7.37836e-05, Final residual = 5.99369e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.12574e-06, global = 3.1245e-06, cumulative = 0.00133995 +smoothSolver: Solving for epsilon, Initial residual = 0.00113615, Final residual = 1.85863e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00214584, Final residual = 4.52028e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.114942 s +other Time = 0 s +rho Equations = 0.000172 s +U Equations = 0.000994 s +Y Equations = 0.00378545 s +E Equations = 0.000899 s +p Equations = 0.003286 s +calculate parcels = 58.4529 s +chemistry correctThermo = 0.003771 s +turbulence correct = 0.001582 s +combustion correct(in Y) = 0.100232 s +percentage of chemistry = 87.2019 % +percentage of rho/U/Y/E = 5.08991 % +========Time details of each equation======= +rhoEqn Time = 0.000411 s +rhoEqn assamble = 0.000332 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000992 s +UEqn assamble = 0.000573 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000419 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.003228 s +YEqn assamble = 0.001059 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000404 s +YEqn correct boundary = 0 s +EEqn Time = 0.000658 s +EEqn assamble = 0.000487 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000171 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 96.79 s ClockTime = 97 s +Courant Number mean: 0.00337345 max: 0.0180518 +Time = 0.00106 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 55 new parcels + +Cloud: sprayCloud + Current number of parcels = 18858 + Current mass in system = 1.46846e-09 + Linear momentum = (3.01811e-11 -1.11795e-08 0) + |Linear momentum| = 1.11795e-08 + Linear kinetic energy = 4.45386e-08 + model1: + number of parcels added = 18879 + mass introduced = 1.52684e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.139, 538.54 + Mass transfer phase change = 5.8373e-11 + D10, D32, Dmax (mu) = 52.7636, 84.4789, 150.655 + Liquid penetration 95% mass (m) = 0.00773248 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00818175, Final residual = 5.576e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0166851, Final residual = 6.51688e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00192073, Final residual = 1.80222e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00340817, Final residual = 3.19671e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00393171, Final residual = 4.01656e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00393173, Final residual = 4.02108e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00282424, Final residual = 1.62427e-07, No Iterations 1 +min/max(T) = 628.778, 1525.38 +GAMG: Solving for p, Initial residual = 0.0461966, Final residual = 6.41305e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.25893e-06, global = 3.13062e-06, cumulative = 0.00134308 +GAMG: Solving for p, Initial residual = 6.40144e-05, Final residual = 4.21568e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.14145e-06, global = 3.14054e-06, cumulative = 0.00134622 +smoothSolver: Solving for epsilon, Initial residual = 0.00114131, Final residual = 1.88288e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00215085, Final residual = 4.56317e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102943 s +other Time = 0 s +rho Equations = 0.00018 s +U Equations = 0.001194 s +Y Equations = 0.00243454 s +E Equations = 0.000627 s +p Equations = 0.002047 s +calculate parcels = 58.7929 s +chemistry correctThermo = 0.002825 s +turbulence correct = 0.001056 s +combustion correct(in Y) = 0.0923725 s +percentage of chemistry = 89.7317 % +percentage of rho/U/Y/E = 4.30874 % +========Time details of each equation======= +rhoEqn Time = 0.000327 s +rhoEqn assamble = 0.000259 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001194 s +UEqn assamble = 0.000685 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000509 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001778 s +YEqn assamble = 0.000641 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000185 s +YEqn correct boundary = 0 s +EEqn Time = 0.000472 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000136 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 97.23 s ClockTime = 98 s +Courant Number mean: 0.00343736 max: 0.0180736 +Time = 0.0010625 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 54 new parcels + +Cloud: sprayCloud + Current number of parcels = 18912 + Current mass in system = 1.47054e-09 + Linear momentum = (3.03339e-11 -1.11866e-08 0) + |Linear momentum| = 1.11866e-08 + Linear kinetic energy = 4.45282e-08 + model1: + number of parcels added = 18933 + mass introduced = 1.52919e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.13, 538.82 + Mass transfer phase change = 5.86469e-11 + D10, D32, Dmax (mu) = 52.625, 84.4944, 150.665 + Liquid penetration 95% mass (m) = 0.00774845 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00762494, Final residual = 5.34501e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0166418, Final residual = 6.54202e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00193375, Final residual = 1.84337e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00342031, Final residual = 3.25825e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00393968, Final residual = 4.08618e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00393969, Final residual = 4.09077e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0028511, Final residual = 1.65507e-07, No Iterations 1 +min/max(T) = 629.314, 1531.32 +GAMG: Solving for p, Initial residual = 0.0460567, Final residual = 5.81032e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.2651e-06, global = 3.14785e-06, cumulative = 0.00134937 +GAMG: Solving for p, Initial residual = 5.72357e-05, Final residual = 3.51251e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.15771e-06, global = 3.15701e-06, cumulative = 0.00135253 +smoothSolver: Solving for epsilon, Initial residual = 0.00114626, Final residual = 1.90649e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00215526, Final residual = 4.60549e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.108029 s +other Time = 1e-06 s +rho Equations = 0.000189 s +U Equations = 0.001179 s +Y Equations = 0.00241629 s +E Equations = 0.00064 s +p Equations = 0.002001 s +calculate parcels = 59.1045 s +chemistry correctThermo = 0.002815 s +turbulence correct = 0.001095 s +combustion correct(in Y) = 0.0974577 s +percentage of chemistry = 90.2144 % +percentage of rho/U/Y/E = 4.09547 % +========Time details of each equation======= +rhoEqn Time = 0.000331 s +rhoEqn assamble = 0.000262 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001178 s +UEqn assamble = 0.000677 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000501 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001739 s +YEqn assamble = 0.000637 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00016 s +YEqn correct boundary = 0 s +EEqn Time = 0.000484 s +EEqn assamble = 0.000366 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 97.65 s ClockTime = 98 s +Courant Number mean: 0.0035016 max: 0.0180877 +Time = 0.001065 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 39 new parcels + +Cloud: sprayCloud + Current number of parcels = 18951 + Current mass in system = 1.47197e-09 + Linear momentum = (3.03839e-11 -1.11894e-08 0) + |Linear momentum| = 1.11894e-08 + Linear kinetic energy = 4.4504e-08 + model1: + number of parcels added = 18972 + mass introduced = 1.53089e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.12, 539.053 + Mass transfer phase change = 5.89223e-11 + D10, D32, Dmax (mu) = 52.5635, 84.5067, 150.674 + Liquid penetration 95% mass (m) = 0.00776475 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00714446, Final residual = 5.12623e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0165843, Final residual = 6.56387e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00194529, Final residual = 1.87239e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00343368, Final residual = 3.31682e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00394937, Final residual = 4.15243e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00394939, Final residual = 4.15708e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00287343, Final residual = 1.67811e-07, No Iterations 1 +min/max(T) = 629.879, 1537.35 +GAMG: Solving for p, Initial residual = 0.0459606, Final residual = 5.66252e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.29109e-06, global = 3.1662e-06, cumulative = 0.00135569 +GAMG: Solving for p, Initial residual = 5.41805e-05, Final residual = 4.81751e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.17467e-06, global = 3.17359e-06, cumulative = 0.00135887 +smoothSolver: Solving for epsilon, Initial residual = 0.00115227, Final residual = 1.93144e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00216168, Final residual = 4.65066e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.081738 s +other Time = 0 s +rho Equations = 0.000197 s +U Equations = 0.001165 s +Y Equations = 0.00239618 s +E Equations = 0.000504 s +p Equations = 0.002134 s +calculate parcels = 59.4602 s +chemistry correctThermo = 0.001907 s +turbulence correct = 0.000935 s +combustion correct(in Y) = 0.0723218 s +percentage of chemistry = 88.48 % +percentage of rho/U/Y/E = 5.21444 % +========Time details of each equation======= +rhoEqn Time = 0.000338 s +rhoEqn assamble = 0.000262 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001163 s +UEqn assamble = 0.000708 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000455 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001613 s +YEqn assamble = 0.00068 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 4.2e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000372 s +EEqn assamble = 0.000281 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 98.09 s ClockTime = 99 s +Courant Number mean: 0.00356641 max: 0.0181116 +Time = 0.0010675 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 18999 + Current mass in system = 1.47377e-09 + Linear momentum = (3.07549e-11 -1.11947e-08 0) + |Linear momentum| = 1.11948e-08 + Linear kinetic energy = 4.44888e-08 + model1: + number of parcels added = 19020 + mass introduced = 1.53297e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.13, 539.247 + Mass transfer phase change = 5.91991e-11 + D10, D32, Dmax (mu) = 52.5552, 84.5249, 150.684 + Liquid penetration 95% mass (m) = 0.00778084 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00685379, Final residual = 4.98056e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0165054, Final residual = 6.58106e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00195214, Final residual = 1.90731e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00344603, Final residual = 3.36716e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00395761, Final residual = 4.20954e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00395764, Final residual = 4.21431e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00289521, Final residual = 1.705e-07, No Iterations 1 +min/max(T) = 630.467, 1542.66 +GAMG: Solving for p, Initial residual = 0.0459188, Final residual = 6.32997e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.33254e-06, global = 3.183e-06, cumulative = 0.00136205 +GAMG: Solving for p, Initial residual = 5.88353e-05, Final residual = 6.44733e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.19271e-06, global = 3.1912e-06, cumulative = 0.00136524 +smoothSolver: Solving for epsilon, Initial residual = 0.00116033, Final residual = 1.96043e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00216951, Final residual = 4.70151e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.083316 s +other Time = 0 s +rho Equations = 0.000162 s +U Equations = 0.001027 s +Y Equations = 0.00245325 s +E Equations = 0.000627 s +p Equations = 0.002187 s +calculate parcels = 59.6956 s +chemistry correctThermo = 0.002843 s +turbulence correct = 0.001055 s +combustion correct(in Y) = 0.0727648 s +percentage of chemistry = 87.3359 % +percentage of rho/U/Y/E = 5.12416 % +========Time details of each equation======= +rhoEqn Time = 0.000317 s +rhoEqn assamble = 0.000251 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001027 s +UEqn assamble = 0.000615 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000412 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001839 s +YEqn assamble = 0.000662 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000202 s +YEqn correct boundary = 0 s +EEqn Time = 0.000468 s +EEqn assamble = 0.000352 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 98.41 s ClockTime = 99 s +Courant Number mean: 0.00363203 max: 0.0181282 +Time = 0.00107 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 55 new parcels + +Cloud: sprayCloud + Current number of parcels = 19054 + Current mass in system = 1.47586e-09 + Linear momentum = (3.12158e-11 -1.12022e-08 0) + |Linear momentum| = 1.12022e-08 + Linear kinetic energy = 4.44809e-08 + model1: + number of parcels added = 19075 + mass introduced = 1.53534e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.144, 539.407 + Mass transfer phase change = 5.94776e-11 + D10, D32, Dmax (mu) = 52.4924, 84.549, 150.693 + Liquid penetration 95% mass (m) = 0.00779691 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0067579, Final residual = 4.97304e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0164099, Final residual = 6.58924e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00195607, Final residual = 1.93586e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0034579, Final residual = 3.41332e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.003965, Final residual = 4.25777e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00396503, Final residual = 4.26257e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00291684, Final residual = 1.73142e-07, No Iterations 1 +min/max(T) = 631.086, 1547.4 +GAMG: Solving for p, Initial residual = 0.0458007, Final residual = 6.45237e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.35655e-06, global = 3.2018e-06, cumulative = 0.00136844 +GAMG: Solving for p, Initial residual = 6.00346e-05, Final residual = 6.47259e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.21136e-06, global = 3.20983e-06, cumulative = 0.00137165 +smoothSolver: Solving for epsilon, Initial residual = 0.00117056, Final residual = 1.99409e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00217885, Final residual = 4.75871e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.089523 s +other Time = 0 s +rho Equations = 0.000146 s +U Equations = 0.000983 s +Y Equations = 0.00213355 s +E Equations = 0.000501 s +p Equations = 0.001742 s +calculate parcels = 59.9855 s +chemistry correctThermo = 0.002029 s +turbulence correct = 0.000848 s +combustion correct(in Y) = 0.0809604 s +percentage of chemistry = 90.4354 % +percentage of rho/U/Y/E = 4.20401 % +========Time details of each equation======= +rhoEqn Time = 0.000285 s +rhoEqn assamble = 0.000229 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000982 s +UEqn assamble = 0.000559 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000423 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001593 s +YEqn assamble = 0.000568 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000152 s +YEqn correct boundary = 0 s +EEqn Time = 0.000378 s +EEqn assamble = 0.000281 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.7e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 98.78 s ClockTime = 99 s +Courant Number mean: 0.00369856 max: 0.0181961 +Time = 0.0010725 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 19104 + Current mass in system = 1.47774e-09 + Linear momentum = (3.08046e-11 -1.12082e-08 0) + |Linear momentum| = 1.12083e-08 + Linear kinetic energy = 4.44689e-08 + model1: + number of parcels added = 19125 + mass introduced = 1.5375e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.125, 539.541 + Mass transfer phase change = 5.97577e-11 + D10, D32, Dmax (mu) = 52.4908, 84.5786, 150.703 + Liquid penetration 95% mass (m) = 0.00781288 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00682514, Final residual = 5.08333e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0163116, Final residual = 6.59477e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00196423, Final residual = 1.964e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00347353, Final residual = 3.44843e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00397717, Final residual = 4.2924e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0039772, Final residual = 4.2972e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0029404, Final residual = 1.75728e-07, No Iterations 1 +min/max(T) = 631.731, 1552.22 +GAMG: Solving for p, Initial residual = 0.0458099, Final residual = 8.96091e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.42846e-06, global = 3.22307e-06, cumulative = 0.00137488 +GAMG: Solving for p, Initial residual = 8.33039e-05, Final residual = 1.64671e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.22862e-06, global = 3.22825e-06, cumulative = 0.0013781 +smoothSolver: Solving for epsilon, Initial residual = 0.00118128, Final residual = 2.03045e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00218906, Final residual = 4.82018e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.086873 s +other Time = 0 s +rho Equations = 0.00016 s +U Equations = 0.001024 s +Y Equations = 0.00199692 s +E Equations = 0.000481 s +p Equations = 0.001794 s +calculate parcels = 60.2994 s +chemistry correctThermo = 0.001994 s +turbulence correct = 0.000803 s +combustion correct(in Y) = 0.0784441 s +percentage of chemistry = 90.2974 % +percentage of rho/U/Y/E = 4.21526 % +========Time details of each equation======= +rhoEqn Time = 0.000274 s +rhoEqn assamble = 0.000221 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001023 s +UEqn assamble = 0.000604 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000419 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001428 s +YEqn assamble = 0.000509 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00012 s +YEqn correct boundary = 0 s +EEqn Time = 0.000367 s +EEqn assamble = 0.000274 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 99.19 s ClockTime = 100 s +Courant Number mean: 0.00376619 max: 0.0184408 +Time = 0.001075 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 45 new parcels + +Cloud: sprayCloud + Current number of parcels = 19149 + Current mass in system = 1.4794e-09 + Linear momentum = (3.07854e-11 -1.12129e-08 0) + |Linear momentum| = 1.1213e-08 + Linear kinetic energy = 4.44526e-08 + model1: + number of parcels added = 19170 + mass introduced = 1.53944e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.144, 539.65 + Mass transfer phase change = 6.00395e-11 + D10, D32, Dmax (mu) = 52.4671, 84.5867, 150.713 + Liquid penetration 95% mass (m) = 0.00782828 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00705246, Final residual = 5.2099e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0162153, Final residual = 6.6043e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00197578, Final residual = 1.99587e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00349459, Final residual = 3.49127e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00399626, Final residual = 4.33647e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00399629, Final residual = 4.34134e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00296457, Final residual = 1.78379e-07, No Iterations 1 +min/max(T) = 632.395, 1557.2 +GAMG: Solving for p, Initial residual = 0.0457463, Final residual = 8.55096e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.42951e-06, global = 3.24084e-06, cumulative = 0.00138135 +GAMG: Solving for p, Initial residual = 7.85193e-05, Final residual = 9.02558e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.24929e-06, global = 3.24778e-06, cumulative = 0.00138459 +smoothSolver: Solving for epsilon, Initial residual = 0.00119395, Final residual = 2.06804e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00219963, Final residual = 4.8851e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.098843 s +other Time = 1e-06 s +rho Equations = 0.000188 s +U Equations = 0.001298 s +Y Equations = 0.00250859 s +E Equations = 0.000608 s +p Equations = 0.001963 s +calculate parcels = 60.6366 s +chemistry correctThermo = 0.002846 s +turbulence correct = 0.000986 s +combustion correct(in Y) = 0.0882454 s +percentage of chemistry = 89.2784 % +percentage of rho/U/Y/E = 4.65647 % +========Time details of each equation======= +rhoEqn Time = 0.00033 s +rhoEqn assamble = 0.00026 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001295 s +UEqn assamble = 0.000762 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000533 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001728 s +YEqn assamble = 0.000636 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000121 s +YEqn correct boundary = 0 s +EEqn Time = 0.000451 s +EEqn assamble = 0.000339 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 99.62 s ClockTime = 100 s +Courant Number mean: 0.0038353 max: 0.0187096 +Time = 0.0010775 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 39 new parcels + +Cloud: sprayCloud + Current number of parcels = 19188 + Current mass in system = 1.4808e-09 + Linear momentum = (3.09861e-11 -1.1216e-08 0) + |Linear momentum| = 1.1216e-08 + Linear kinetic energy = 4.44314e-08 + model1: + number of parcels added = 19209 + mass introduced = 1.54112e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.125, 539.746 + Mass transfer phase change = 6.0323e-11 + D10, D32, Dmax (mu) = 52.4665, 84.6149, 150.722 + Liquid penetration 95% mass (m) = 0.00784287 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00749073, Final residual = 5.48765e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0161368, Final residual = 6.64077e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00198729, Final residual = 2.01964e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00351699, Final residual = 3.53625e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00401713, Final residual = 4.38648e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00401716, Final residual = 4.39138e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00298576, Final residual = 1.81164e-07, No Iterations 1 +min/max(T) = 633.077, 1562.28 +GAMG: Solving for p, Initial residual = 0.0458406, Final residual = 9.70581e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.4906e-06, global = 3.25878e-06, cumulative = 0.00138785 +GAMG: Solving for p, Initial residual = 8.79109e-05, Final residual = 9.58933e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.26964e-06, global = 3.2678e-06, cumulative = 0.00139112 +smoothSolver: Solving for epsilon, Initial residual = 0.00120671, Final residual = 2.10791e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0022113, Final residual = 4.95537e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.088096 s +other Time = 0 s +rho Equations = 0.000179 s +U Equations = 0.001167 s +Y Equations = 0.00243573 s +E Equations = 0.000604 s +p Equations = 0.002366 s +calculate parcels = 60.9456 s +chemistry correctThermo = 0.003066 s +turbulence correct = 0.001078 s +combustion correct(in Y) = 0.0769853 s +percentage of chemistry = 87.3879 % +percentage of rho/U/Y/E = 4.97835 % +========Time details of each equation======= +rhoEqn Time = 0.000356 s +rhoEqn assamble = 0.000273 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001166 s +UEqn assamble = 0.000675 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000491 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001794 s +YEqn assamble = 0.000635 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000204 s +YEqn correct boundary = 0 s +EEqn Time = 0.000446 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 100.02 s ClockTime = 101 s +Courant Number mean: 0.00390613 max: 0.0189924 +Time = 0.00108 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 53 new parcels + +Cloud: sprayCloud + Current number of parcels = 19241 + Current mass in system = 1.48278e-09 + Linear momentum = (3.08551e-11 -1.1223e-08 0) + |Linear momentum| = 1.1223e-08 + Linear kinetic energy = 4.44238e-08 + model1: + number of parcels added = 19262 + mass introduced = 1.54339e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.129, 539.867 + Mass transfer phase change = 6.06084e-11 + D10, D32, Dmax (mu) = 52.4613, 84.6339, 150.732 + Liquid penetration 95% mass (m) = 0.00785861 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00817758, Final residual = 6.00564e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0160801, Final residual = 6.70732e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00199198, Final residual = 2.05193e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0035378, Final residual = 3.58007e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00403565, Final residual = 4.43246e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00403568, Final residual = 4.43735e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00300808, Final residual = 1.83733e-07, No Iterations 1 +min/max(T) = 633.78, 1567.44 +GAMG: Solving for p, Initial residual = 0.0459639, Final residual = 9.74838e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.52794e-06, global = 3.28032e-06, cumulative = 0.0013944 +GAMG: Solving for p, Initial residual = 8.92823e-05, Final residual = 1.76825e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.29031e-06, global = 3.28991e-06, cumulative = 0.00139769 +smoothSolver: Solving for epsilon, Initial residual = 0.00122072, Final residual = 2.15094e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00222455, Final residual = 5.03207e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095223 s +other Time = 0 s +rho Equations = 0.000171 s +U Equations = 0.001177 s +Y Equations = 0.00208495 s +E Equations = 0.000494 s +p Equations = 0.00186 s +calculate parcels = 61.2479 s +chemistry correctThermo = 0.002022 s +turbulence correct = 0.00081 s +combustion correct(in Y) = 0.08641 s +percentage of chemistry = 90.7449 % +percentage of rho/U/Y/E = 4.12396 % +========Time details of each equation======= +rhoEqn Time = 0.00029 s +rhoEqn assamble = 0.000232 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001176 s +UEqn assamble = 0.000674 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000502 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001415 s +YEqn assamble = 0.00052 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.5e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000373 s +EEqn assamble = 0.00028 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 100.42 s ClockTime = 101 s +Courant Number mean: 0.00397882 max: 0.0192774 +Time = 0.0010825 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 56 new parcels + +Cloud: sprayCloud + Current number of parcels = 19297 + Current mass in system = 1.48488e-09 + Linear momentum = (3.07892e-11 -1.12309e-08 0) + |Linear momentum| = 1.1231e-08 + Linear kinetic energy = 4.44198e-08 + model1: + number of parcels added = 19318 + mass introduced = 1.54578e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.131, 539.956 + Mass transfer phase change = 6.08959e-11 + D10, D32, Dmax (mu) = 52.4511, 84.6521, 150.742 + Liquid penetration 95% mass (m) = 0.00787344 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00891927, Final residual = 6.69703e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0160374, Final residual = 6.77987e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00199616, Final residual = 2.09489e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00355221, Final residual = 3.61838e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00404552, Final residual = 4.47119e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00404556, Final residual = 4.47602e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00303504, Final residual = 1.87081e-07, No Iterations 1 +min/max(T) = 634.511, 1572.66 +GAMG: Solving for p, Initial residual = 0.0460902, Final residual = 0.000102644, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.56721e-06, global = 3.29979e-06, cumulative = 0.00140099 +GAMG: Solving for p, Initial residual = 9.45117e-05, Final residual = 1.94671e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.31416e-06, global = 3.31367e-06, cumulative = 0.0014043 +smoothSolver: Solving for epsilon, Initial residual = 0.001237, Final residual = 2.19821e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0022389, Final residual = 5.11313e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.091507 s +other Time = 0 s +rho Equations = 0.000165 s +U Equations = 0.001197 s +Y Equations = 0.00230648 s +E Equations = 0.000569 s +p Equations = 0.001864 s +calculate parcels = 61.4906 s +chemistry correctThermo = 0.00194 s +turbulence correct = 0.000936 s +combustion correct(in Y) = 0.0823415 s +percentage of chemistry = 89.9839 % +percentage of rho/U/Y/E = 4.63077 % +========Time details of each equation======= +rhoEqn Time = 0.000288 s +rhoEqn assamble = 0.000231 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001196 s +UEqn assamble = 0.000703 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000493 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001725 s +YEqn assamble = 0.000621 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000165 s +YEqn correct boundary = 0 s +EEqn Time = 0.000403 s +EEqn assamble = 0.000305 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 100.75 s ClockTime = 101 s +Courant Number mean: 0.00405316 max: 0.0195543 +Time = 0.001085 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 19345 + Current mass in system = 1.4867e-09 + Linear momentum = (3.06961e-11 -1.12371e-08 0) + |Linear momentum| = 1.12371e-08 + Linear kinetic energy = 4.44104e-08 + model1: + number of parcels added = 19367 + mass introduced = 1.54788e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.148, 540.023 + Mass transfer phase change = 6.11865e-11 + D10, D32, Dmax (mu) = 52.7086, 84.6637, 150.752 + Liquid penetration 95% mass (m) = 0.00788879 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00951943, Final residual = 7.32579e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0159956, Final residual = 6.84079e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00200998, Final residual = 2.14496e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00356947, Final residual = 3.64601e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00405765, Final residual = 4.50422e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00405769, Final residual = 4.50925e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00307023, Final residual = 1.91583e-07, No Iterations 1 +min/max(T) = 635.273, 1591.31 +GAMG: Solving for p, Initial residual = 0.0460547, Final residual = 8.21171e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.53858e-06, global = 3.34047e-06, cumulative = 0.00140764 +GAMG: Solving for p, Initial residual = 7.76756e-05, Final residual = 7.10676e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.35054e-06, global = 3.34912e-06, cumulative = 0.00141099 +smoothSolver: Solving for epsilon, Initial residual = 0.00125399, Final residual = 2.24515e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00225349, Final residual = 5.19309e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.098124 s +other Time = 0 s +rho Equations = 0.000171 s +U Equations = 0.001212 s +Y Equations = 0.00251059 s +E Equations = 0.000613 s +p Equations = 0.002076 s +calculate parcels = 61.7706 s +chemistry correctThermo = 0.002831 s +turbulence correct = 0.000957 s +combustion correct(in Y) = 0.0875574 s +percentage of chemistry = 89.2314 % +percentage of rho/U/Y/E = 4.59275 % +========Time details of each equation======= +rhoEqn Time = 0.000317 s +rhoEqn assamble = 0.00025 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001212 s +UEqn assamble = 0.000733 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000479 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001862 s +YEqn assamble = 0.000667 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000203 s +YEqn correct boundary = 0 s +EEqn Time = 0.000451 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 101.13 s ClockTime = 102 s +Courant Number mean: 0.00412873 max: 0.0199217 +Time = 0.0010875 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 60 new parcels + +Cloud: sprayCloud + Current number of parcels = 19405 + Current mass in system = 1.489e-09 + Linear momentum = (3.08542e-11 -1.12467e-08 0) + |Linear momentum| = 1.12468e-08 + Linear kinetic energy = 4.4414e-08 + model1: + number of parcels added = 19427 + mass introduced = 1.55048e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.135, 540.071 + Mass transfer phase change = 6.14782e-11 + D10, D32, Dmax (mu) = 52.698, 84.6752, 150.762 + Liquid penetration 95% mass (m) = 0.0079053 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00966971, Final residual = 7.56253e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0159423, Final residual = 6.8861e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00201485, Final residual = 2.16695e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00358743, Final residual = 3.67891e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00407313, Final residual = 4.53539e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00407318, Final residual = 4.5405e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0031015, Final residual = 1.94881e-07, No Iterations 1 +min/max(T) = 636.058, 1614.87 +GAMG: Solving for p, Initial residual = 0.0461822, Final residual = 0.000102445, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.58924e-06, global = 3.35341e-06, cumulative = 0.00141435 +GAMG: Solving for p, Initial residual = 9.62755e-05, Final residual = 3.38529e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.3631e-06, global = 3.36249e-06, cumulative = 0.00141771 +smoothSolver: Solving for epsilon, Initial residual = 0.0012698, Final residual = 2.28746e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00226675, Final residual = 5.26717e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.098474 s +other Time = 1e-06 s +rho Equations = 0.00021 s +U Equations = 0.0014 s +Y Equations = 0.00241265 s +E Equations = 0.000645 s +p Equations = 0.002247 s +calculate parcels = 62.084 s +chemistry correctThermo = 0.002778 s +turbulence correct = 0.000997 s +combustion correct(in Y) = 0.0875504 s +percentage of chemistry = 88.9071 % +percentage of rho/U/Y/E = 4.73998 % +========Time details of each equation======= +rhoEqn Time = 0.000353 s +rhoEqn assamble = 0.000277 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001399 s +UEqn assamble = 0.000847 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000552 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001681 s +YEqn assamble = 0.00062 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000135 s +YEqn correct boundary = 0 s +EEqn Time = 0.000489 s +EEqn assamble = 0.00037 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000119 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 101.54 s ClockTime = 102 s +Courant Number mean: 0.0042054 max: 0.0202861 +Time = 0.00109 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 19455 + Current mass in system = 1.49095e-09 + Linear momentum = (3.03728e-11 -1.12543e-08 0) + |Linear momentum| = 1.12544e-08 + Linear kinetic energy = 4.44117e-08 + model1: + number of parcels added = 19478 + mass introduced = 1.55272e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.131, 540.106 + Mass transfer phase change = 6.17732e-11 + D10, D32, Dmax (mu) = 52.8287, 84.6747, 150.772 + Liquid penetration 95% mass (m) = 0.00792234 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00964185, Final residual = 7.54262e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0158927, Final residual = 6.93351e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00203488, Final residual = 2.2183e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00360652, Final residual = 3.75507e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00408772, Final residual = 4.62997e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00408777, Final residual = 4.63536e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00313475, Final residual = 1.98501e-07, No Iterations 1 +min/max(T) = 636.86, 1638.34 +GAMG: Solving for p, Initial residual = 0.046262, Final residual = 0.000103907, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.6334e-06, global = 3.38809e-06, cumulative = 0.0014211 +GAMG: Solving for p, Initial residual = 9.72601e-05, Final residual = 3.16087e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.40026e-06, global = 3.39964e-06, cumulative = 0.0014245 +smoothSolver: Solving for epsilon, Initial residual = 0.00128455, Final residual = 2.32744e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0022792, Final residual = 5.33925e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.105659 s +other Time = 0 s +rho Equations = 0.000179 s +U Equations = 0.001248 s +Y Equations = 0.00222048 s +E Equations = 0.000636 s +p Equations = 0.002199 s +calculate parcels = 62.4002 s +chemistry correctThermo = 0.002787 s +turbulence correct = 0.001022 s +combustion correct(in Y) = 0.0951695 s +percentage of chemistry = 90.0723 % +percentage of rho/U/Y/E = 4.05406 % +========Time details of each equation======= +rhoEqn Time = 0.000323 s +rhoEqn assamble = 0.000258 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001248 s +UEqn assamble = 0.000749 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000499 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001582 s +YEqn assamble = 0.000551 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000109 s +YEqn correct boundary = 0 s +EEqn Time = 0.000511 s +EEqn assamble = 0.000352 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000159 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 101.96 s ClockTime = 102 s +Courant Number mean: 0.00428294 max: 0.0205969 +Time = 0.0010925 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 19505 + Current mass in system = 1.49288e-09 + Linear momentum = (3.06977e-11 -1.1262e-08 0) + |Linear momentum| = 1.12621e-08 + Linear kinetic energy = 4.44108e-08 + model1: + number of parcels added = 19528 + mass introduced = 1.55495e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.139, 540.131 + Mass transfer phase change = 6.20695e-11 + D10, D32, Dmax (mu) = 52.8364, 84.7077, 150.783 + Liquid penetration 95% mass (m) = 0.00793836 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00952388, Final residual = 7.56155e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0158695, Final residual = 6.98995e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00204093, Final residual = 2.27005e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00363208, Final residual = 3.82088e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0041129, Final residual = 4.70919e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00411295, Final residual = 4.71466e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00316221, Final residual = 2.02406e-07, No Iterations 1 +min/max(T) = 637.702, 1661.66 +GAMG: Solving for p, Initial residual = 0.0464451, Final residual = 0.000102213, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.66049e-06, global = 3.40683e-06, cumulative = 0.0014279 +GAMG: Solving for p, Initial residual = 9.5091e-05, Final residual = 1.86902e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.41539e-06, global = 3.41492e-06, cumulative = 0.00143132 +smoothSolver: Solving for epsilon, Initial residual = 0.00129749, Final residual = 2.36791e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00229174, Final residual = 5.41795e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.091748 s +other Time = 0 s +rho Equations = 0.000159 s +U Equations = 0.001108 s +Y Equations = 0.00202934 s +E Equations = 0.00049 s +p Equations = 0.001748 s +calculate parcels = 62.7075 s +chemistry correctThermo = 0.002011 s +turbulence correct = 0.000856 s +combustion correct(in Y) = 0.0831597 s +percentage of chemistry = 90.6392 % +percentage of rho/U/Y/E = 4.12689 % +========Time details of each equation======= +rhoEqn Time = 0.000274 s +rhoEqn assamble = 0.000215 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001108 s +UEqn assamble = 0.000679 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000429 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001463 s +YEqn assamble = 0.000526 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000136 s +YEqn correct boundary = 0 s +EEqn Time = 0.000371 s +EEqn assamble = 0.000276 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 102.36 s ClockTime = 103 s +Courant Number mean: 0.0043614 max: 0.0209981 +Time = 0.001095 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 55 new parcels + +Cloud: sprayCloud + Current number of parcels = 19560 + Current mass in system = 1.49505e-09 + Linear momentum = (3.09465e-11 -1.12717e-08 0) + |Linear momentum| = 1.12717e-08 + Linear kinetic energy = 4.44178e-08 + model1: + number of parcels added = 19583 + mass introduced = 1.55742e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.149, 540.15 + Mass transfer phase change = 6.23685e-11 + D10, D32, Dmax (mu) = 52.7528, 84.7225, 150.793 + Liquid penetration 95% mass (m) = 0.00795479 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00928453, Final residual = 7.68023e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0158386, Final residual = 7.0686e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00205885, Final residual = 2.32023e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00366006, Final residual = 3.89055e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00413953, Final residual = 4.78677e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00413959, Final residual = 4.7925e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00319127, Final residual = 2.06225e-07, No Iterations 1 +min/max(T) = 638.574, 1684.73 +GAMG: Solving for p, Initial residual = 0.0466983, Final residual = 9.494e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.68792e-06, global = 3.43505e-06, cumulative = 0.00143475 +GAMG: Solving for p, Initial residual = 8.62889e-05, Final residual = 2.79956e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.44699e-06, global = 3.44631e-06, cumulative = 0.0014382 +smoothSolver: Solving for epsilon, Initial residual = 0.00130933, Final residual = 2.40701e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00230522, Final residual = 5.50235e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.075435 s +other Time = 0 s +rho Equations = 0.000147 s +U Equations = 0.001089 s +Y Equations = 0.00239538 s +E Equations = 0.000494 s +p Equations = 0.001917 s +calculate parcels = 63.0209 s +chemistry correctThermo = 0.002118 s +turbulence correct = 0.000852 s +combustion correct(in Y) = 0.0662376 s +percentage of chemistry = 87.8075 % +percentage of rho/U/Y/E = 5.46879 % +========Time details of each equation======= +rhoEqn Time = 0.000302 s +rhoEqn assamble = 0.000227 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001089 s +UEqn assamble = 0.000646 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000443 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001831 s +YEqn assamble = 0.000636 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000193 s +YEqn correct boundary = 0 s +EEqn Time = 0.000372 s +EEqn assamble = 0.000275 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.7e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 102.75 s ClockTime = 103 s +Courant Number mean: 0.00444103 max: 0.0213018 +Time = 0.0010975 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 52 new parcels + +Cloud: sprayCloud + Current number of parcels = 19612 + Current mass in system = 1.49711e-09 + Linear momentum = (3.13078e-11 -1.12809e-08 0) + |Linear momentum| = 1.1281e-08 + Linear kinetic energy = 4.44245e-08 + model1: + number of parcels added = 19635 + mass introduced = 1.55978e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.137, 540.165 + Mass transfer phase change = 6.26705e-11 + D10, D32, Dmax (mu) = 52.7569, 84.7489, 150.803 + Liquid penetration 95% mass (m) = 0.00796948 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00919682, Final residual = 7.90228e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0158399, Final residual = 7.18193e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00207746, Final residual = 2.37675e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00368748, Final residual = 3.96687e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00416498, Final residual = 4.87554e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00416503, Final residual = 4.88151e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0032204, Final residual = 2.09924e-07, No Iterations 1 +min/max(T) = 639.47, 1707.41 +GAMG: Solving for p, Initial residual = 0.0469558, Final residual = 8.25023e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.70045e-06, global = 3.46878e-06, cumulative = 0.00144167 +GAMG: Solving for p, Initial residual = 7.38044e-05, Final residual = 2.27857e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.48123e-06, global = 3.48066e-06, cumulative = 0.00144515 +smoothSolver: Solving for epsilon, Initial residual = 0.00132189, Final residual = 2.44678e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00231967, Final residual = 5.59279e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.072468 s +other Time = 0 s +rho Equations = 0.000185 s +U Equations = 0.001076 s +Y Equations = 0.00237283 s +E Equations = 0.000492 s +p Equations = 0.001863 s +calculate parcels = 63.3013 s +chemistry correctThermo = 0.001951 s +turbulence correct = 0.000838 s +combustion correct(in Y) = 0.0634802 s +percentage of chemistry = 87.5975 % +percentage of rho/U/Y/E = 5.69332 % +========Time details of each equation======= +rhoEqn Time = 0.000309 s +rhoEqn assamble = 0.000247 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001075 s +UEqn assamble = 0.00065 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000425 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001781 s +YEqn assamble = 0.000604 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000135 s +YEqn correct boundary = 0 s +EEqn Time = 0.00037 s +EEqn assamble = 0.00028 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 103.1 s ClockTime = 104 s +Courant Number mean: 0.00452196 max: 0.0215881 +Time = 0.0011 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 19658 + Current mass in system = 1.49893e-09 + Linear momentum = (3.13504e-11 -1.12887e-08 0) + |Linear momentum| = 1.12887e-08 + Linear kinetic energy = 4.44268e-08 + model1: + number of parcels added = 19681 + mass introduced = 1.5619e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.144, 540.175 + Mass transfer phase change = 6.29757e-11 + D10, D32, Dmax (mu) = 52.7274, 84.7632, 150.814 + Liquid penetration 95% mass (m) = 0.00798381 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00919908, Final residual = 8.21817e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0158459, Final residual = 7.30565e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00209154, Final residual = 2.42599e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00371425, Final residual = 4.04572e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00418906, Final residual = 4.9638e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00418912, Final residual = 4.9698e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00325258, Final residual = 2.14233e-07, No Iterations 1 +min/max(T) = 640.393, 1729.52 +GAMG: Solving for p, Initial residual = 0.0472025, Final residual = 7.51312e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.7185e-06, global = 3.50598e-06, cumulative = 0.00144866 +GAMG: Solving for p, Initial residual = 6.91041e-05, Final residual = 8.15489e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.51992e-06, global = 3.51779e-06, cumulative = 0.00145217 +smoothSolver: Solving for epsilon, Initial residual = 0.0013344, Final residual = 2.48644e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00233442, Final residual = 5.68765e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.087351 s +other Time = 0 s +rho Equations = 0.000173 s +U Equations = 0.001245 s +Y Equations = 0.00237679 s +E Equations = 0.000596 s +p Equations = 0.002038 s +calculate parcels = 63.5855 s +chemistry correctThermo = 0.002791 s +turbulence correct = 0.000941 s +combustion correct(in Y) = 0.0770042 s +percentage of chemistry = 88.1549 % +percentage of rho/U/Y/E = 5.0266 % +========Time details of each equation======= +rhoEqn Time = 0.000326 s +rhoEqn assamble = 0.000258 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001245 s +UEqn assamble = 0.000742 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000503 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001712 s +YEqn assamble = 0.000639 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000182 s +YEqn correct boundary = 0 s +EEqn Time = 0.000443 s +EEqn assamble = 0.000323 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00012 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 103.78 s ClockTime = 104 s +Courant Number mean: 0.00460429 max: 0.0219642 +Time = 0.0011025 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 37 new parcels + +Cloud: sprayCloud + Current number of parcels = 19695 + Current mass in system = 1.50033e-09 + Linear momentum = (3.13554e-11 -1.12939e-08 0) + |Linear momentum| = 1.12939e-08 + Linear kinetic energy = 4.44212e-08 + model1: + number of parcels added = 19718 + mass introduced = 1.56362e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.173, 540.183 + Mass transfer phase change = 6.32842e-11 + D10, D32, Dmax (mu) = 52.7291, 84.7823, 150.824 + Liquid penetration 95% mass (m) = 0.00800012 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00925432, Final residual = 8.49859e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0158398, Final residual = 7.4273e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00211369, Final residual = 2.4899e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00373993, Final residual = 4.124e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00421153, Final residual = 5.05013e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00421159, Final residual = 5.05618e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00328679, Final residual = 2.18991e-07, No Iterations 1 +min/max(T) = 641.346, 1750.89 +GAMG: Solving for p, Initial residual = 0.0474449, Final residual = 7.67911e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.7589e-06, global = 3.54473e-06, cumulative = 0.00145572 +GAMG: Solving for p, Initial residual = 7.10607e-05, Final residual = 6.37721e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.55792e-06, global = 3.55635e-06, cumulative = 0.00145927 +smoothSolver: Solving for epsilon, Initial residual = 0.0013459, Final residual = 2.52631e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00234845, Final residual = 5.78823e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103402 s +other Time = 1e-06 s +rho Equations = 0.000181 s +U Equations = 0.001254 s +Y Equations = 0.00295447 s +E Equations = 0.000675 s +p Equations = 0.002189 s +calculate parcels = 63.8965 s +chemistry correctThermo = 0.002859 s +turbulence correct = 0.001291 s +combustion correct(in Y) = 0.0917845 s +percentage of chemistry = 88.7648 % +percentage of rho/U/Y/E = 4.89784 % +========Time details of each equation======= +rhoEqn Time = 0.000333 s +rhoEqn assamble = 0.000265 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001254 s +UEqn assamble = 0.000754 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.0005 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002321 s +YEqn assamble = 0.00079 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000244 s +YEqn correct boundary = 0 s +EEqn Time = 0.000496 s +EEqn assamble = 0.000373 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000123 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 104.2 s ClockTime = 105 s +Courant Number mean: 0.00468797 max: 0.0223509 +Time = 0.001105 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 56 new parcels + +Cloud: sprayCloud + Current number of parcels = 19750 + Current mass in system = 1.50263e-09 + Linear momentum = (3.16397e-11 -1.13057e-08 0) + |Linear momentum| = 1.13057e-08 + Linear kinetic energy = 4.44405e-08 + model1: + number of parcels added = 19774 + mass introduced = 1.56623e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.143, 540.188 + Mass transfer phase change = 6.35972e-11 + D10, D32, Dmax (mu) = 52.9811, 84.8111, 150.835 + Liquid penetration 95% mass (m) = 0.00801645 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00934255, Final residual = 8.68624e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0158215, Final residual = 7.5393e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00214099, Final residual = 2.57168e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00376466, Final residual = 4.20211e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0042317, Final residual = 5.13317e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00423177, Final residual = 5.13925e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00332401, Final residual = 2.24102e-07, No Iterations 1 +min/max(T) = 642.329, 1771.46 +GAMG: Solving for p, Initial residual = 0.0476582, Final residual = 7.23959e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.80009e-06, global = 3.59647e-06, cumulative = 0.00146287 +GAMG: Solving for p, Initial residual = 6.85091e-05, Final residual = 7.09174e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.60894e-06, global = 3.60725e-06, cumulative = 0.00146648 +smoothSolver: Solving for epsilon, Initial residual = 0.00135713, Final residual = 2.56738e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00236158, Final residual = 5.8918e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095783 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001259 s +Y Equations = 0.00258144 s +E Equations = 0.000687 s +p Equations = 0.002488 s +calculate parcels = 64.2059 s +chemistry correctThermo = 0.002853 s +turbulence correct = 0.001051 s +combustion correct(in Y) = 0.0844646 s +percentage of chemistry = 88.1833 % +percentage of rho/U/Y/E = 4.91156 % +========Time details of each equation======= +rhoEqn Time = 0.000344 s +rhoEqn assamble = 0.000272 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001258 s +UEqn assamble = 0.000758 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.0005 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001929 s +YEqn assamble = 0.000696 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000201 s +YEqn correct boundary = 0 s +EEqn Time = 0.000497 s +EEqn assamble = 0.000376 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000121 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 104.6 s ClockTime = 105 s +Courant Number mean: 0.00477309 max: 0.0227552 +Time = 0.0011075 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 59 new parcels + +Cloud: sprayCloud + Current number of parcels = 19809 + Current mass in system = 1.5051e-09 + Linear momentum = (3.10085e-11 -1.1319e-08 0) + |Linear momentum| = 1.13191e-08 + Linear kinetic energy = 4.44666e-08 + model1: + number of parcels added = 19833 + mass introduced = 1.56901e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.141, 540.192 + Mass transfer phase change = 6.39126e-11 + D10, D32, Dmax (mu) = 52.9635, 84.8226, 150.846 + Liquid penetration 95% mass (m) = 0.00803195 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00935755, Final residual = 8.84951e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0158057, Final residual = 7.64468e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00214878, Final residual = 2.61234e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00378661, Final residual = 4.27709e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00425068, Final residual = 5.2153e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00425076, Final residual = 5.22154e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00335882, Final residual = 2.28782e-07, No Iterations 1 +min/max(T) = 643.343, 1791.14 +GAMG: Solving for p, Initial residual = 0.0478757, Final residual = 6.58336e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.80771e-06, global = 3.62312e-06, cumulative = 0.0014701 +GAMG: Solving for p, Initial residual = 6.17373e-05, Final residual = 7.28413e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.63641e-06, global = 3.63473e-06, cumulative = 0.00147374 +smoothSolver: Solving for epsilon, Initial residual = 0.00136964, Final residual = 2.61475e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00237571, Final residual = 6.00126e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.099343 s +other Time = 1e-06 s +rho Equations = 0.000174 s +U Equations = 0.001323 s +Y Equations = 0.00237081 s +E Equations = 0.000598 s +p Equations = 0.002112 s +calculate parcels = 64.5446 s +chemistry correctThermo = 0.002821 s +turbulence correct = 0.000957 s +combustion correct(in Y) = 0.0887822 s +percentage of chemistry = 89.3693 % +percentage of rho/U/Y/E = 4.49535 % +========Time details of each equation======= +rhoEqn Time = 0.000328 s +rhoEqn assamble = 0.000259 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001321 s +UEqn assamble = 0.000814 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000507 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001734 s +YEqn assamble = 0.00063 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000175 s +YEqn correct boundary = 0 s +EEqn Time = 0.000446 s +EEqn assamble = 0.000333 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 105.04 s ClockTime = 106 s +Courant Number mean: 0.00485959 max: 0.0233661 +Time = 0.00111 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 19853 + Current mass in system = 1.50689e-09 + Linear momentum = (3.15687e-11 -1.13277e-08 0) + |Linear momentum| = 1.13278e-08 + Linear kinetic energy = 4.44768e-08 + model1: + number of parcels added = 19877 + mass introduced = 1.57112e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.159, 540.195 + Mass transfer phase change = 6.42314e-11 + D10, D32, Dmax (mu) = 52.9689, 84.8487, 150.857 + Liquid penetration 95% mass (m) = 0.00804847 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00928161, Final residual = 9.06201e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0158088, Final residual = 7.7601e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00216435, Final residual = 2.67111e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0038079, Final residual = 4.35226e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00426769, Final residual = 5.29873e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00426777, Final residual = 5.305e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00339528, Final residual = 2.33887e-07, No Iterations 1 +min/max(T) = 644.392, 1809.86 +GAMG: Solving for p, Initial residual = 0.0480797, Final residual = 5.89067e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.83495e-06, global = 3.66264e-06, cumulative = 0.0014774 +GAMG: Solving for p, Initial residual = 5.62497e-05, Final residual = 4.78057e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.67646e-06, global = 3.67522e-06, cumulative = 0.00148107 +smoothSolver: Solving for epsilon, Initial residual = 0.00138178, Final residual = 2.66618e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00239209, Final residual = 6.11936e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.072977 s +other Time = 0 s +rho Equations = 0.000171 s +U Equations = 0.00124 s +Y Equations = 0.00240723 s +E Equations = 0.000496 s +p Equations = 0.001868 s +calculate parcels = 64.852 s +chemistry correctThermo = 0.001996 s +turbulence correct = 0.000853 s +combustion correct(in Y) = 0.0637448 s +percentage of chemistry = 87.3491 % +percentage of rho/U/Y/E = 5.91177 % +========Time details of each equation======= +rhoEqn Time = 0.000301 s +rhoEqn assamble = 0.000242 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001239 s +UEqn assamble = 0.000778 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000461 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001784 s +YEqn assamble = 0.000592 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000158 s +YEqn correct boundary = 0 s +EEqn Time = 0.00037 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 105.42 s ClockTime = 106 s +Courant Number mean: 0.00494739 max: 0.0239388 +Time = 0.0011125 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 55 new parcels + +Cloud: sprayCloud + Current number of parcels = 19908 + Current mass in system = 1.50922e-09 + Linear momentum = (3.12224e-11 -1.13408e-08 0) + |Linear momentum| = 1.13408e-08 + Linear kinetic energy = 4.4504e-08 + model1: + number of parcels added = 19932 + mass introduced = 1.57377e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.156, 540.197 + Mass transfer phase change = 6.4554e-11 + D10, D32, Dmax (mu) = 52.9788, 84.8899, 150.868 + Liquid penetration 95% mass (m) = 0.00806453 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00912009, Final residual = 9.21556e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0158168, Final residual = 7.8743e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00218512, Final residual = 2.7307e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00382843, Final residual = 4.42647e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0042836, Final residual = 5.38147e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00428369, Final residual = 5.38806e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00343432, Final residual = 2.39236e-07, No Iterations 1 +min/max(T) = 645.473, 1827.57 +GAMG: Solving for p, Initial residual = 0.0482805, Final residual = 6.48441e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.8946e-06, global = 3.7039e-06, cumulative = 0.00148478 +GAMG: Solving for p, Initial residual = 6.21854e-05, Final residual = 4.98993e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.71889e-06, global = 3.71753e-06, cumulative = 0.00148849 +smoothSolver: Solving for epsilon, Initial residual = 0.00139377, Final residual = 2.72216e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00240913, Final residual = 6.24646e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092742 s +other Time = 1e-06 s +rho Equations = 0.000191 s +U Equations = 0.001408 s +Y Equations = 0.00252024 s +E Equations = 0.000612 s +p Equations = 0.001691 s +calculate parcels = 65.131 s +chemistry correctThermo = 0.002303 s +turbulence correct = 0.000824 s +combustion correct(in Y) = 0.0829858 s +percentage of chemistry = 89.4802 % +percentage of rho/U/Y/E = 5.10151 % +========Time details of each equation======= +rhoEqn Time = 0.00031 s +rhoEqn assamble = 0.000243 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001406 s +UEqn assamble = 0.000851 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000555 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001762 s +YEqn assamble = 0.000666 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000137 s +YEqn correct boundary = 0 s +EEqn Time = 0.000453 s +EEqn assamble = 0.000339 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 105.79 s ClockTime = 106 s +Courant Number mean: 0.00503621 max: 0.024459 +Time = 0.001115 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 55 new parcels + +Cloud: sprayCloud + Current number of parcels = 19963 + Current mass in system = 1.51157e-09 + Linear momentum = (3.10008e-11 -1.13542e-08 0) + |Linear momentum| = 1.13543e-08 + Linear kinetic energy = 4.45343e-08 + model1: + number of parcels added = 19987 + mass introduced = 1.57645e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.154, 540.198 + Mass transfer phase change = 6.48804e-11 + D10, D32, Dmax (mu) = 52.9861, 84.9176, 150.879 + Liquid penetration 95% mass (m) = 0.0080798 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00892075, Final residual = 9.345e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0158263, Final residual = 7.98799e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00220086, Final residual = 2.79805e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00384737, Final residual = 4.50469e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00429736, Final residual = 5.47395e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00429745, Final residual = 5.48075e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00347453, Final residual = 2.4505e-07, No Iterations 1 +min/max(T) = 646.583, 1844.27 +GAMG: Solving for p, Initial residual = 0.0484601, Final residual = 6.88289e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.94545e-06, global = 3.74847e-06, cumulative = 0.00149224 +GAMG: Solving for p, Initial residual = 6.69594e-05, Final residual = 5.55616e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.76348e-06, global = 3.76204e-06, cumulative = 0.00149601 +smoothSolver: Solving for epsilon, Initial residual = 0.0014076, Final residual = 2.78073e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0024264, Final residual = 6.37426e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.089639 s +other Time = 0 s +rho Equations = 0.000174 s +U Equations = 0.001266 s +Y Equations = 0.00299769 s +E Equations = 0.000736 s +p Equations = 0.002236 s +calculate parcels = 65.4745 s +chemistry correctThermo = 0.003146 s +turbulence correct = 0.000934 s +combustion correct(in Y) = 0.0778993 s +percentage of chemistry = 86.9034 % +percentage of rho/U/Y/E = 5.77169 % +========Time details of each equation======= +rhoEqn Time = 0.000321 s +rhoEqn assamble = 0.000257 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001265 s +UEqn assamble = 0.000769 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000496 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002315 s +YEqn assamble = 0.000809 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00032 s +YEqn correct boundary = 0 s +EEqn Time = 0.000549 s +EEqn assamble = 0.000416 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000133 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 106.23 s ClockTime = 107 s +Courant Number mean: 0.0051259 max: 0.0249537 +Time = 0.0011175 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 57 new parcels + +Cloud: sprayCloud + Current number of parcels = 20020 + Current mass in system = 1.51405e-09 + Linear momentum = (3.09777e-11 -1.1369e-08 0) + |Linear momentum| = 1.13691e-08 + Linear kinetic energy = 4.45703e-08 + model1: + number of parcels added = 20044 + mass introduced = 1.57926e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.155, 540.199 + Mass transfer phase change = 6.52108e-11 + D10, D32, Dmax (mu) = 52.9944, 84.9452, 150.891 + Liquid penetration 95% mass (m) = 0.00809447 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00862922, Final residual = 9.4012e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0158275, Final residual = 8.09388e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0022182, Final residual = 2.85399e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00386507, Final residual = 4.60044e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00430949, Final residual = 5.57554e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00430959, Final residual = 5.58254e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00351397, Final residual = 2.50892e-07, No Iterations 1 +min/max(T) = 646.466, 1860.02 +GAMG: Solving for p, Initial residual = 0.0486336, Final residual = 6.82677e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.98986e-06, global = 3.79417e-06, cumulative = 0.0014998 +GAMG: Solving for p, Initial residual = 6.85985e-05, Final residual = 5.49076e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.80903e-06, global = 3.80766e-06, cumulative = 0.00150361 +smoothSolver: Solving for epsilon, Initial residual = 0.00142078, Final residual = 2.83852e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00244477, Final residual = 6.50036e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.104929 s +other Time = 0 s +rho Equations = 0.000179 s +U Equations = 0.001221 s +Y Equations = 0.00244971 s +E Equations = 0.000597 s +p Equations = 0.00211 s +calculate parcels = 65.8037 s +chemistry correctThermo = 0.002827 s +turbulence correct = 0.001072 s +combustion correct(in Y) = 0.0942833 s +percentage of chemistry = 89.8544 % +percentage of rho/U/Y/E = 4.23782 % +========Time details of each equation======= +rhoEqn Time = 0.000335 s +rhoEqn assamble = 0.000261 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001219 s +UEqn assamble = 0.000725 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000494 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001793 s +YEqn assamble = 0.000656 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000194 s +YEqn correct boundary = 0 s +EEqn Time = 0.000442 s +EEqn assamble = 0.000329 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 106.66 s ClockTime = 107 s +Courant Number mean: 0.00521626 max: 0.0253952 +Time = 0.00112 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 42 new parcels + +Cloud: sprayCloud + Current number of parcels = 20062 + Current mass in system = 1.51582e-09 + Linear momentum = (3.15984e-11 -1.13787e-08 0) + |Linear momentum| = 1.13787e-08 + Linear kinetic energy = 4.4588e-08 + model1: + number of parcels added = 20086 + mass introduced = 1.58136e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.159, 540.2 + Mass transfer phase change = 6.55451e-11 + D10, D32, Dmax (mu) = 52.9938, 84.9666, 150.902 + Liquid penetration 95% mass (m) = 0.00811102 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00828046, Final residual = 9.34607e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0158126, Final residual = 8.18477e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00223515, Final residual = 2.89981e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0038808, Final residual = 4.7042e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0043193, Final residual = 5.68976e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0043194, Final residual = 5.6969e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0035537, Final residual = 2.56331e-07, No Iterations 1 +min/max(T) = 646.371, 1874.87 +GAMG: Solving for p, Initial residual = 0.0487855, Final residual = 6.87373e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.04116e-06, global = 3.83973e-06, cumulative = 0.00150745 +GAMG: Solving for p, Initial residual = 6.93648e-05, Final residual = 5.65841e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.85516e-06, global = 3.85369e-06, cumulative = 0.0015113 +smoothSolver: Solving for epsilon, Initial residual = 0.00143267, Final residual = 2.89433e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00246156, Final residual = 6.62604e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092873 s +other Time = 0 s +rho Equations = 0.000172 s +U Equations = 0.001304 s +Y Equations = 0.00242581 s +E Equations = 0.000639 s +p Equations = 0.002053 s +calculate parcels = 66.1055 s +chemistry correctThermo = 0.00282 s +turbulence correct = 0.000997 s +combustion correct(in Y) = 0.0822552 s +percentage of chemistry = 88.5674 % +percentage of rho/U/Y/E = 4.88927 % +========Time details of each equation======= +rhoEqn Time = 0.000311 s +rhoEqn assamble = 0.000248 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001304 s +UEqn assamble = 0.000799 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000505 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001788 s +YEqn assamble = 0.000651 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000175 s +YEqn correct boundary = 0 s +EEqn Time = 0.000471 s +EEqn assamble = 0.000347 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000124 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 107.05 s ClockTime = 108 s +Courant Number mean: 0.00530722 max: 0.0257914 +Time = 0.0011225 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 55 new parcels + +Cloud: sprayCloud + Current number of parcels = 20117 + Current mass in system = 1.51824e-09 + Linear momentum = (3.15977e-11 -1.13936e-08 0) + |Linear momentum| = 1.13937e-08 + Linear kinetic energy = 4.46269e-08 + model1: + number of parcels added = 20141 + mass introduced = 1.58413e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.153, 540.2 + Mass transfer phase change = 6.58835e-11 + D10, D32, Dmax (mu) = 52.9738, 84.9863, 150.914 + Liquid penetration 95% mass (m) = 0.0081276 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00793684, Final residual = 9.22232e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0157804, Final residual = 8.25806e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00225946, Final residual = 2.96442e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00389401, Final residual = 4.80528e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00432604, Final residual = 5.79187e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00432615, Final residual = 5.79908e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00359431, Final residual = 2.6159e-07, No Iterations 1 +min/max(T) = 646.326, 1888.91 +GAMG: Solving for p, Initial residual = 0.0489018, Final residual = 7.27591e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.10051e-06, global = 3.8857e-06, cumulative = 0.00151519 +GAMG: Solving for p, Initial residual = 7.31327e-05, Final residual = 7.22106e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.90247e-06, global = 3.90048e-06, cumulative = 0.00151909 +smoothSolver: Solving for epsilon, Initial residual = 0.00144356, Final residual = 2.95054e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00247702, Final residual = 6.74932e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094654 s +other Time = 0 s +rho Equations = 0.000173 s +U Equations = 0.001309 s +Y Equations = 0.00353548 s +E Equations = 0.000929 s +p Equations = 0.003083 s +calculate parcels = 66.4475 s +chemistry correctThermo = 0.005313 s +turbulence correct = 0.000826 s +combustion correct(in Y) = 0.0792795 s +percentage of chemistry = 83.7572 % +percentage of rho/U/Y/E = 6.28234 % +========Time details of each equation======= +rhoEqn Time = 0.000381 s +rhoEqn assamble = 0.000287 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001308 s +UEqn assamble = 0.000787 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000521 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002753 s +YEqn assamble = 0.000981 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000449 s +YEqn correct boundary = 0 s +EEqn Time = 0.000696 s +EEqn assamble = 0.000502 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000194 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 107.49 s ClockTime = 108 s +Courant Number mean: 0.00539865 max: 0.0261637 +Time = 0.001125 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 52 new parcels + +Cloud: sprayCloud + Current number of parcels = 20169 + Current mass in system = 1.52055e-09 + Linear momentum = (3.13369e-11 -1.14079e-08 0) + |Linear momentum| = 1.14079e-08 + Linear kinetic energy = 4.46643e-08 + model1: + number of parcels added = 20193 + mass introduced = 1.58677e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.15, 540.2 + Mass transfer phase change = 6.62261e-11 + D10, D32, Dmax (mu) = 52.9684, 85.0114, 150.926 + Liquid penetration 95% mass (m) = 0.00814364 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00760105, Final residual = 9.04833e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0157311, Final residual = 8.31577e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00227858, Final residual = 3.02147e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00390383, Final residual = 4.89468e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00432876, Final residual = 5.88787e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00432889, Final residual = 5.89536e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00363341, Final residual = 2.66708e-07, No Iterations 1 +min/max(T) = 646.317, 1902.2 +GAMG: Solving for p, Initial residual = 0.0489889, Final residual = 7.33966e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.15508e-06, global = 3.93326e-06, cumulative = 0.00152302 +GAMG: Solving for p, Initial residual = 7.50299e-05, Final residual = 7.43845e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.95014e-06, global = 3.94797e-06, cumulative = 0.00152697 +smoothSolver: Solving for epsilon, Initial residual = 0.00145346, Final residual = 3.00942e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00249093, Final residual = 6.8693e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.074063 s +other Time = 0 s +rho Equations = 0.00018 s +U Equations = 0.001198 s +Y Equations = 0.00258037 s +E Equations = 0.00051 s +p Equations = 0.001789 s +calculate parcels = 66.7557 s +chemistry correctThermo = 0.001938 s +turbulence correct = 0.000917 s +combustion correct(in Y) = 0.0647326 s +percentage of chemistry = 87.4021 % +percentage of rho/U/Y/E = 6.0332 % +========Time details of each equation======= +rhoEqn Time = 0.000304 s +rhoEqn assamble = 0.000238 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001197 s +UEqn assamble = 0.000769 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000428 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001958 s +YEqn assamble = 0.000738 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00014 s +YEqn correct boundary = 0 s +EEqn Time = 0.000382 s +EEqn assamble = 0.000287 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 107.87 s ClockTime = 108 s +Courant Number mean: 0.0054904 max: 0.0265283 +Time = 0.0011275 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 45 new parcels + +Cloud: sprayCloud + Current number of parcels = 20214 + Current mass in system = 1.5225e-09 + Linear momentum = (3.1323e-11 -1.14197e-08 0) + |Linear momentum| = 1.14197e-08 + Linear kinetic energy = 4.46923e-08 + model1: + number of parcels added = 20238 + mass introduced = 1.58907e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.162, 540.2 + Mass transfer phase change = 6.65728e-11 + D10, D32, Dmax (mu) = 52.9559, 85.0209, 150.938 + Liquid penetration 95% mass (m) = 0.00815878 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00722024, Final residual = 8.79368e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0156607, Final residual = 8.34759e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00229763, Final residual = 3.07208e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0039108, Final residual = 4.97726e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00432809, Final residual = 5.9698e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00432822, Final residual = 5.97733e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00367167, Final residual = 2.72181e-07, No Iterations 1 +min/max(T) = 646.357, 1914.84 +GAMG: Solving for p, Initial residual = 0.0490417, Final residual = 7.19124e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.20442e-06, global = 3.98169e-06, cumulative = 0.00153095 +GAMG: Solving for p, Initial residual = 7.30578e-05, Final residual = 6.63904e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.99846e-06, global = 3.99633e-06, cumulative = 0.00153495 +smoothSolver: Solving for epsilon, Initial residual = 0.00146269, Final residual = 3.06853e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00250311, Final residual = 6.98421e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097338 s +other Time = 1e-06 s +rho Equations = 0.000175 s +U Equations = 0.00126 s +Y Equations = 0.00292823 s +E Equations = 0.00075 s +p Equations = 0.002716 s +calculate parcels = 67.0453 s +chemistry correctThermo = 0.00317 s +turbulence correct = 0.001588 s +combustion correct(in Y) = 0.0844428 s +percentage of chemistry = 86.7521 % +percentage of rho/U/Y/E = 5.25306 % +========Time details of each equation======= +rhoEqn Time = 0.000483 s +rhoEqn assamble = 0.000305 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000178 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001259 s +UEqn assamble = 0.00077 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000489 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002289 s +YEqn assamble = 0.000818 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000259 s +YEqn correct boundary = 0 s +EEqn Time = 0.00057 s +EEqn assamble = 0.000434 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000136 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 108.26 s ClockTime = 109 s +Courant Number mean: 0.00558237 max: 0.027034 +Time = 0.00113 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 20262 + Current mass in system = 1.52465e-09 + Linear momentum = (3.12386e-11 -1.1433e-08 0) + |Linear momentum| = 1.1433e-08 + Linear kinetic energy = 4.47267e-08 + model1: + number of parcels added = 20287 + mass introduced = 1.59157e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.165, 540.2 + Mass transfer phase change = 6.69247e-11 + D10, D32, Dmax (mu) = 53.1698, 85.0381, 150.95 + Liquid penetration 95% mass (m) = 0.00817445 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00680494, Final residual = 8.51458e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0155646, Final residual = 8.35157e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00232324, Final residual = 3.13641e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00391427, Final residual = 5.04208e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00432251, Final residual = 6.03434e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00432265, Final residual = 6.04181e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00370914, Final residual = 2.78216e-07, No Iterations 1 +min/max(T) = 646.436, 1926.92 +GAMG: Solving for p, Initial residual = 0.0491154, Final residual = 7.94414e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.28428e-06, global = 4.0379e-06, cumulative = 0.00153898 +GAMG: Solving for p, Initial residual = 7.99023e-05, Final residual = 8.07392e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.0583e-06, global = 4.0557e-06, cumulative = 0.00154304 +smoothSolver: Solving for epsilon, Initial residual = 0.00147131, Final residual = 3.12827e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0025132, Final residual = 7.09297e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.104264 s +other Time = 0 s +rho Equations = 0.000196 s +U Equations = 0.001177 s +Y Equations = 0.0024773 s +E Equations = 0.0006 s +p Equations = 0.002081 s +calculate parcels = 67.382 s +chemistry correctThermo = 0.002814 s +turbulence correct = 0.000967 s +combustion correct(in Y) = 0.0937047 s +percentage of chemistry = 89.8725 % +percentage of rho/U/Y/E = 4.2683 % +========Time details of each equation======= +rhoEqn Time = 0.000344 s +rhoEqn assamble = 0.000272 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001176 s +UEqn assamble = 0.000739 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000437 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001903 s +YEqn assamble = 0.000741 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00022 s +YEqn correct boundary = 0 s +EEqn Time = 0.000449 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 108.7 s ClockTime = 109 s +Courant Number mean: 0.00567448 max: 0.0275777 +Time = 0.0011325 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 43 new parcels + +Cloud: sprayCloud + Current number of parcels = 20304 + Current mass in system = 1.52648e-09 + Linear momentum = (3.10741e-11 -1.1444e-08 0) + |Linear momentum| = 1.1444e-08 + Linear kinetic energy = 4.4752e-08 + model1: + number of parcels added = 20330 + mass introduced = 1.59376e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.152, 540.2 + Mass transfer phase change = 6.72802e-11 + D10, D32, Dmax (mu) = 53.4113, 85.0644, 150.963 + Liquid penetration 95% mass (m) = 0.00819074 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00633617, Final residual = 8.18699e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0154465, Final residual = 8.32336e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00232374, Final residual = 3.16036e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00390584, Final residual = 5.07644e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00430393, Final residual = 6.05937e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00430407, Final residual = 6.06666e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00374328, Final residual = 2.82783e-07, No Iterations 1 +min/max(T) = 646.545, 1938.53 +GAMG: Solving for p, Initial residual = 0.0492122, Final residual = 0.000111623, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.43398e-06, global = 4.06248e-06, cumulative = 0.0015471 +GAMG: Solving for p, Initial residual = 0.000108155, Final residual = 2.69529e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.09828e-06, global = 4.09739e-06, cumulative = 0.0015512 +smoothSolver: Solving for epsilon, Initial residual = 0.00148218, Final residual = 3.1931e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00252142, Final residual = 7.19582e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102817 s +other Time = 0 s +rho Equations = 0.000171 s +U Equations = 0.001292 s +Y Equations = 0.00240203 s +E Equations = 0.000607 s +p Equations = 0.002259 s +calculate parcels = 67.6952 s +chemistry correctThermo = 0.00285 s +turbulence correct = 0.001073 s +combustion correct(in Y) = 0.091956 s +percentage of chemistry = 89.4365 % +percentage of rho/U/Y/E = 4.34951 % +========Time details of each equation======= +rhoEqn Time = 0.000318 s +rhoEqn assamble = 0.00025 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001291 s +UEqn assamble = 0.000799 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000492 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001773 s +YEqn assamble = 0.000641 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000186 s +YEqn correct boundary = 0 s +EEqn Time = 0.000448 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 109.12 s ClockTime = 110 s +Courant Number mean: 0.0057666 max: 0.0283868 +Time = 0.001135 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 45 new parcels + +Cloud: sprayCloud + Current number of parcels = 20348 + Current mass in system = 1.52841e-09 + Linear momentum = (3.0795e-11 -1.14557e-08 0) + |Linear momentum| = 1.14558e-08 + Linear kinetic energy = 4.47805e-08 + model1: + number of parcels added = 20375 + mass introduced = 1.59605e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.156, 540.197 + Mass transfer phase change = 6.7639e-11 + D10, D32, Dmax (mu) = 53.6453, 85.0788, 150.976 + Liquid penetration 95% mass (m) = 0.00820477 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00594252, Final residual = 7.82551e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0153045, Final residual = 8.23326e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00231983, Final residual = 3.17934e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00388709, Final residual = 5.07123e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00427291, Final residual = 6.03989e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00427306, Final residual = 6.04702e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00377969, Final residual = 2.87473e-07, No Iterations 1 +min/max(T) = 646.685, 1949.68 +GAMG: Solving for p, Initial residual = 0.0491687, Final residual = 0.00015605, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.58886e-06, global = 4.07845e-06, cumulative = 0.00155528 +GAMG: Solving for p, Initial residual = 0.000150539, Final residual = 3.688e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.13681e-06, global = 4.13559e-06, cumulative = 0.00155941 +smoothSolver: Solving for epsilon, Initial residual = 0.00149415, Final residual = 3.26497e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00252565, Final residual = 7.2896e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103052 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001312 s +Y Equations = 0.00242001 s +E Equations = 0.000631 s +p Equations = 0.00226 s +calculate parcels = 68.0354 s +chemistry correctThermo = 0.002783 s +turbulence correct = 0.001063 s +combustion correct(in Y) = 0.09221 s +percentage of chemistry = 89.4791 % +percentage of rho/U/Y/E = 4.40556 % +========Time details of each equation======= +rhoEqn Time = 0.000345 s +rhoEqn assamble = 0.000276 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001311 s +UEqn assamble = 0.000811 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.0005 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001785 s +YEqn assamble = 0.000629 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000191 s +YEqn correct boundary = 0 s +EEqn Time = 0.000478 s +EEqn assamble = 0.00034 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000138 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 109.56 s ClockTime = 110 s +Courant Number mean: 0.00585812 max: 0.0287845 +Time = 0.0011375 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 20399 + Current mass in system = 1.53064e-09 + Linear momentum = (3.14784e-11 -1.14698e-08 0) + |Linear momentum| = 1.14698e-08 + Linear kinetic energy = 4.48183e-08 + model1: + number of parcels added = 20426 + mass introduced = 1.59864e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.159, 540.199 + Mass transfer phase change = 6.79999e-11 + D10, D32, Dmax (mu) = 53.6243, 85.092, 150.988 + Liquid penetration 95% mass (m) = 0.00822086 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0054954, Final residual = 7.43186e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0151444, Final residual = 8.11066e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00231246, Final residual = 3.16269e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00387814, Final residual = 5.02189e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00425535, Final residual = 5.97188e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0042555, Final residual = 5.97878e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00381348, Final residual = 2.91716e-07, No Iterations 1 +min/max(T) = 646.848, 1960.37 +GAMG: Solving for p, Initial residual = 0.049003, Final residual = 0.000150167, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.57873e-06, global = 4.13011e-06, cumulative = 0.00156354 +GAMG: Solving for p, Initial residual = 0.000140824, Final residual = 3.83078e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.1601e-06, global = 4.15899e-06, cumulative = 0.0015677 +smoothSolver: Solving for epsilon, Initial residual = 0.00150309, Final residual = 3.32836e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00252407, Final residual = 7.36189e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09616 s +other Time = 0 s +rho Equations = 0.000165 s +U Equations = 0.001246 s +Y Equations = 0.00244908 s +E Equations = 0.000513 s +p Equations = 0.001936 s +calculate parcels = 68.3513 s +chemistry correctThermo = 0.002041 s +turbulence correct = 0.000938 s +combustion correct(in Y) = 0.0866789 s +percentage of chemistry = 90.1403 % +percentage of rho/U/Y/E = 4.54771 % +========Time details of each equation======= +rhoEqn Time = 0.000305 s +rhoEqn assamble = 0.000244 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001245 s +UEqn assamble = 0.000795 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00045 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001801 s +YEqn assamble = 0.000669 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000176 s +YEqn correct boundary = 0 s +EEqn Time = 0.00039 s +EEqn assamble = 0.000289 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000101 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 109.97 s ClockTime = 110 s +Courant Number mean: 0.00594863 max: 0.0294862 +Time = 0.00114 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 40 new parcels + +Cloud: sprayCloud + Current number of parcels = 20438 + Current mass in system = 1.5323e-09 + Linear momentum = (3.15466e-11 -1.14796e-08 0) + |Linear momentum| = 1.14796e-08 + Linear kinetic energy = 4.48395e-08 + model1: + number of parcels added = 20466 + mass introduced = 1.60067e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.165, 540.2 + Mass transfer phase change = 6.83639e-11 + D10, D32, Dmax (mu) = 53.8973, 85.1253, 151.001 + Liquid penetration 95% mass (m) = 0.0082366 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00465483, Final residual = 6.40459e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0149403, Final residual = 7.98004e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00231893, Final residual = 3.17548e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00388011, Final residual = 5.02266e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00425096, Final residual = 5.96561e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00425112, Final residual = 5.97245e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00383269, Final residual = 2.95585e-07, No Iterations 1 +min/max(T) = 647.033, 1970.73 +GAMG: Solving for p, Initial residual = 0.0489334, Final residual = 0.000153625, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.57908e-06, global = 4.17983e-06, cumulative = 0.00157188 +GAMG: Solving for p, Initial residual = 0.000141905, Final residual = 3.5077e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.19698e-06, global = 4.19623e-06, cumulative = 0.00157608 +smoothSolver: Solving for epsilon, Initial residual = 0.00150818, Final residual = 3.37568e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00252053, Final residual = 7.42125e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.085472 s +other Time = 0 s +rho Equations = 0.000176 s +U Equations = 0.001211 s +Y Equations = 0.00225972 s +E Equations = 0.000499 s +p Equations = 0.001931 s +calculate parcels = 68.6363 s +chemistry correctThermo = 0.001929 s +turbulence correct = 0.001043 s +combustion correct(in Y) = 0.0762293 s +percentage of chemistry = 89.1863 % +percentage of rho/U/Y/E = 4.85038 % +========Time details of each equation======= +rhoEqn Time = 0.000309 s +rhoEqn assamble = 0.000245 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00121 s +UEqn assamble = 0.000778 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000432 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001641 s +YEqn assamble = 0.000585 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000159 s +YEqn correct boundary = 0 s +EEqn Time = 0.000375 s +EEqn assamble = 0.000284 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 110.34 s ClockTime = 111 s +Courant Number mean: 0.0060385 max: 0.0298969 +Time = 0.0011425 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 52 new parcels + +Cloud: sprayCloud + Current number of parcels = 20490 + Current mass in system = 1.53457e-09 + Linear momentum = (3.15727e-11 -1.1494e-08 0) + |Linear momentum| = 1.14941e-08 + Linear kinetic energy = 4.48792e-08 + model1: + number of parcels added = 20518 + mass introduced = 1.60329e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.145, 540.2 + Mass transfer phase change = 6.87294e-11 + D10, D32, Dmax (mu) = 53.887, 85.1398, 151.015 + Liquid penetration 95% mass (m) = 0.00825258 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00429939, Final residual = 5.73578e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0147293, Final residual = 7.88633e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00231443, Final residual = 3.18842e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00388648, Final residual = 5.0548e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00425439, Final residual = 5.99166e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00425456, Final residual = 5.99863e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00383997, Final residual = 2.97555e-07, No Iterations 1 +min/max(T) = 647.253, 1980.94 +GAMG: Solving for p, Initial residual = 0.0491889, Final residual = 0.000147425, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.66655e-06, global = 4.19297e-06, cumulative = 0.00158027 +GAMG: Solving for p, Initial residual = 0.000133443, Final residual = 2.97834e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.21326e-06, global = 4.21251e-06, cumulative = 0.00158448 +smoothSolver: Solving for epsilon, Initial residual = 0.00151066, Final residual = 3.41361e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00251978, Final residual = 7.48593e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.110439 s +other Time = 0 s +rho Equations = 0.00018 s +U Equations = 0.001296 s +Y Equations = 0.00240597 s +E Equations = 0.000606 s +p Equations = 0.001881 s +calculate parcels = 68.9376 s +chemistry correctThermo = 0.002169 s +turbulence correct = 0.000884 s +combustion correct(in Y) = 0.100791 s +percentage of chemistry = 91.264 % +percentage of rho/U/Y/E = 4.06376 % +========Time details of each equation======= +rhoEqn Time = 0.000307 s +rhoEqn assamble = 0.000242 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001294 s +UEqn assamble = 0.000797 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000497 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001745 s +YEqn assamble = 0.000626 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000189 s +YEqn correct boundary = 0 s +EEqn Time = 0.000453 s +EEqn assamble = 0.00034 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 110.76 s ClockTime = 111 s +Courant Number mean: 0.00612922 max: 0.0302701 +Time = 0.001145 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 61 new parcels + +Cloud: sprayCloud + Current number of parcels = 20551 + Current mass in system = 1.53728e-09 + Linear momentum = (3.19152e-11 -1.1512e-08 0) + |Linear momentum| = 1.15121e-08 + Linear kinetic energy = 4.4933e-08 + model1: + number of parcels added = 20579 + mass introduced = 1.60638e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.15, 540.2 + Mass transfer phase change = 6.90977e-11 + D10, D32, Dmax (mu) = 53.8884, 85.1786, 151.028 + Liquid penetration 95% mass (m) = 0.00826894 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0046002, Final residual = 6.28324e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0145448, Final residual = 7.86666e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00232864, Final residual = 3.22108e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00389277, Final residual = 5.08944e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00425662, Final residual = 6.02661e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00425679, Final residual = 6.03361e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00384661, Final residual = 2.99985e-07, No Iterations 1 +min/max(T) = 647.5, 1991.08 +GAMG: Solving for p, Initial residual = 0.0495408, Final residual = 0.000159977, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.78126e-06, global = 4.21738e-06, cumulative = 0.0015887 +GAMG: Solving for p, Initial residual = 0.000144714, Final residual = 2.78293e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.24632e-06, global = 4.24549e-06, cumulative = 0.00159295 +smoothSolver: Solving for epsilon, Initial residual = 0.00151621, Final residual = 3.45671e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00252459, Final residual = 7.57327e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.093229 s +other Time = 0 s +rho Equations = 0.000172 s +U Equations = 0.001449 s +Y Equations = 0.0023396 s +E Equations = 0.000537 s +p Equations = 0.002272 s +calculate parcels = 69.2137 s +chemistry correctThermo = 0.002042 s +turbulence correct = 0.001057 s +combustion correct(in Y) = 0.0831514 s +percentage of chemistry = 89.1905 % +percentage of rho/U/Y/E = 4.82425 % +========Time details of each equation======= +rhoEqn Time = 0.000338 s +rhoEqn assamble = 0.000272 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001448 s +UEqn assamble = 0.000896 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000552 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001684 s +YEqn assamble = 0.000594 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000113 s +YEqn correct boundary = 0 s +EEqn Time = 0.000402 s +EEqn assamble = 0.000305 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.7e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 111.13 s ClockTime = 112 s +Courant Number mean: 0.00622208 max: 0.0306668 +Time = 0.0011475 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 35 new parcels + +Cloud: sprayCloud + Current number of parcels = 20586 + Current mass in system = 1.53869e-09 + Linear momentum = (3.17942e-11 -1.152e-08 0) + |Linear momentum| = 1.152e-08 + Linear kinetic energy = 4.49477e-08 + model1: + number of parcels added = 20614 + mass introduced = 1.60816e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.152, 540.2 + Mass transfer phase change = 6.94694e-11 + D10, D32, Dmax (mu) = 53.8807, 85.2039, 151.042 + Liquid penetration 95% mass (m) = 0.00828585 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00544408, Final residual = 7.72752e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0144126, Final residual = 7.92762e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00233781, Final residual = 3.25619e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00389927, Final residual = 5.1159e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00425828, Final residual = 6.0591e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00425846, Final residual = 6.06613e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00386122, Final residual = 3.03617e-07, No Iterations 1 +min/max(T) = 647.779, 2001.14 +GAMG: Solving for p, Initial residual = 0.0499242, Final residual = 0.000164156, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.8412e-06, global = 4.25792e-06, cumulative = 0.00159721 +GAMG: Solving for p, Initial residual = 0.000150942, Final residual = 2.15169e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.28477e-06, global = 4.28408e-06, cumulative = 0.00160149 +smoothSolver: Solving for epsilon, Initial residual = 0.00152513, Final residual = 3.5067e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00253665, Final residual = 7.68127e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.111462 s +other Time = 1e-06 s +rho Equations = 0.000194 s +U Equations = 0.001407 s +Y Equations = 0.00298342 s +E Equations = 0.000751 s +p Equations = 0.002709 s +calculate parcels = 69.5276 s +chemistry correctThermo = 0.003023 s +turbulence correct = 0.001114 s +combustion correct(in Y) = 0.0990646 s +percentage of chemistry = 88.8774 % +percentage of rho/U/Y/E = 4.78676 % +========Time details of each equation======= +rhoEqn Time = 0.000362 s +rhoEqn assamble = 0.000279 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001405 s +UEqn assamble = 0.000859 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000546 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002289 s +YEqn assamble = 0.00085 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000241 s +YEqn correct boundary = 0 s +EEqn Time = 0.000566 s +EEqn assamble = 0.000437 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000129 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 111.55 s ClockTime = 112 s +Courant Number mean: 0.00631768 max: 0.0310832 +Time = 0.00115 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 65 new parcels + +Cloud: sprayCloud + Current number of parcels = 20650 + Current mass in system = 1.54159e-09 + Linear momentum = (3.20113e-11 -1.15396e-08 0) + |Linear momentum| = 1.15396e-08 + Linear kinetic energy = 4.50082e-08 + model1: + number of parcels added = 20679 + mass introduced = 1.61144e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.153, 540.2 + Mass transfer phase change = 6.98458e-11 + D10, D32, Dmax (mu) = 54.0842, 85.2384, 151.055 + Liquid penetration 95% mass (m) = 0.00830229 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00663833, Final residual = 9.447e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.01431, Final residual = 8.00726e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0023513, Final residual = 3.29596e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00390341, Final residual = 5.14811e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00425551, Final residual = 6.09026e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0042557, Final residual = 6.09706e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00388781, Final residual = 3.08587e-07, No Iterations 1 +min/max(T) = 648.102, 2011.47 +GAMG: Solving for p, Initial residual = 0.0502705, Final residual = 0.000152992, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.85595e-06, global = 4.31732e-06, cumulative = 0.00160581 +GAMG: Solving for p, Initial residual = 0.000142656, Final residual = 1.86257e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.33849e-06, global = 4.33792e-06, cumulative = 0.00161014 +smoothSolver: Solving for epsilon, Initial residual = 0.00153496, Final residual = 3.55756e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00254992, Final residual = 7.79704e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.101348 s +other Time = 0 s +rho Equations = 0.000207 s +U Equations = 0.001273 s +Y Equations = 0.00342831 s +E Equations = 0.000945 s +p Equations = 0.002194 s +calculate parcels = 69.8824 s +chemistry correctThermo = 0.002677 s +turbulence correct = 0.000967 s +combustion correct(in Y) = 0.0894037 s +percentage of chemistry = 88.2146 % +percentage of rho/U/Y/E = 5.77546 % +========Time details of each equation======= +rhoEqn Time = 0.000344 s +rhoEqn assamble = 0.000273 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001271 s +UEqn assamble = 0.000776 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000495 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002765 s +YEqn assamble = 0.001006 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000499 s +YEqn correct boundary = 0 s +EEqn Time = 0.000714 s +EEqn assamble = 0.000516 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000198 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 112.01 s ClockTime = 112 s +Courant Number mean: 0.00641573 max: 0.0314437 +Time = 0.0011525 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 57 new parcels + +Cloud: sprayCloud + Current number of parcels = 20706 + Current mass in system = 1.5441e-09 + Linear momentum = (3.21665e-11 -1.15563e-08 0) + |Linear momentum| = 1.15563e-08 + Linear kinetic energy = 4.50573e-08 + model1: + number of parcels added = 20736 + mass introduced = 1.61433e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.148, 540.2 + Mass transfer phase change = 7.02256e-11 + D10, D32, Dmax (mu) = 54.2307, 85.2751, 151.07 + Liquid penetration 95% mass (m) = 0.00831887 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00782532, Final residual = 1.08995e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0141883, Final residual = 8.06232e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00235547, Final residual = 3.31995e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0039014, Final residual = 5.1706e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00424611, Final residual = 6.10726e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0042463, Final residual = 6.11434e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0039211, Final residual = 3.13886e-07, No Iterations 1 +min/max(T) = 648.455, 2022.29 +GAMG: Solving for p, Initial residual = 0.050618, Final residual = 0.000139673, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.83566e-06, global = 4.35686e-06, cumulative = 0.0016145 +GAMG: Solving for p, Initial residual = 0.000131973, Final residual = 1.34086e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.37859e-06, global = 4.3782e-06, cumulative = 0.00161888 +smoothSolver: Solving for epsilon, Initial residual = 0.00154592, Final residual = 3.60197e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00256175, Final residual = 7.9036e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.10379 s +other Time = 0 s +rho Equations = 0.00015 s +U Equations = 0.001084 s +Y Equations = 0.00263735 s +E Equations = 0.000658 s +p Equations = 0.002486 s +calculate parcels = 70.2474 s +chemistry correctThermo = 0.003027 s +turbulence correct = 0.001154 s +combustion correct(in Y) = 0.0923687 s +percentage of chemistry = 88.9957 % +percentage of rho/U/Y/E = 4.36395 % +========Time details of each equation======= +rhoEqn Time = 0.000309 s +rhoEqn assamble = 0.000243 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001084 s +UEqn assamble = 0.000674 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00041 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002088 s +YEqn assamble = 0.000725 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000289 s +YEqn correct boundary = 0 s +EEqn Time = 0.00049 s +EEqn assamble = 0.00036 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00013 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 112.48 s ClockTime = 113 s +Courant Number mean: 0.00651553 max: 0.0316921 +Time = 0.001155 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 41 new parcels + +Cloud: sprayCloud + Current number of parcels = 20747 + Current mass in system = 1.54581e-09 + Linear momentum = (3.19041e-11 -1.15667e-08 0) + |Linear momentum| = 1.15668e-08 + Linear kinetic energy = 4.50823e-08 + model1: + number of parcels added = 20777 + mass introduced = 1.61642e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.15, 540.2 + Mass transfer phase change = 7.06078e-11 + D10, D32, Dmax (mu) = 54.2222, 85.2973, 151.084 + Liquid penetration 95% mass (m) = 0.00833545 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00871397, Final residual = 1.18676e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0140517, Final residual = 8.08641e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00235814, Final residual = 3.34457e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00390311, Final residual = 5.1805e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00424236, Final residual = 6.11347e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00424257, Final residual = 6.12062e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00395693, Final residual = 3.20426e-07, No Iterations 1 +min/max(T) = 648.837, 2033.13 +GAMG: Solving for p, Initial residual = 0.0509249, Final residual = 0.000118009, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.75998e-06, global = 4.39402e-06, cumulative = 0.00162327 +GAMG: Solving for p, Initial residual = 0.000112262, Final residual = 2.15516e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.40484e-06, global = 4.40434e-06, cumulative = 0.00162768 +smoothSolver: Solving for epsilon, Initial residual = 0.0015569, Final residual = 3.64572e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00257348, Final residual = 8.00469e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.073742 s +other Time = 0 s +rho Equations = 0.000163 s +U Equations = 0.001086 s +Y Equations = 0.00231422 s +E Equations = 0.000545 s +p Equations = 0.001903 s +calculate parcels = 70.5117 s +chemistry correctThermo = 0.002115 s +turbulence correct = 0.000862 s +combustion correct(in Y) = 0.0645538 s +percentage of chemistry = 87.54 % +percentage of rho/U/Y/E = 5.57107 % +========Time details of each equation======= +rhoEqn Time = 0.000291 s +rhoEqn assamble = 0.000231 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001084 s +UEqn assamble = 0.000682 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000402 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001752 s +YEqn assamble = 0.000648 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000154 s +YEqn correct boundary = 0 s +EEqn Time = 0.000417 s +EEqn assamble = 0.000318 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 112.81 s ClockTime = 113 s +Courant Number mean: 0.00661623 max: 0.031859 +Time = 0.0011575 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 38 new parcels + +Cloud: sprayCloud + Current number of parcels = 20785 + Current mass in system = 1.54735e-09 + Linear momentum = (3.20485e-11 -1.1576e-08 0) + |Linear momentum| = 1.1576e-08 + Linear kinetic energy = 4.51027e-08 + model1: + number of parcels added = 20815 + mass introduced = 1.61834e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.166, 540.2 + Mass transfer phase change = 7.0993e-11 + D10, D32, Dmax (mu) = 54.1769, 85.3035, 151.098 + Liquid penetration 95% mass (m) = 0.00835137 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00902449, Final residual = 1.22297e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0139035, Final residual = 8.08819e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00236239, Final residual = 3.35869e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00390679, Final residual = 5.21467e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0042409, Final residual = 6.13984e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00424111, Final residual = 6.14744e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00399125, Final residual = 3.26256e-07, No Iterations 1 +min/max(T) = 649.25, 2043.98 +GAMG: Solving for p, Initial residual = 0.0513208, Final residual = 0.000122203, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.79947e-06, global = 4.42771e-06, cumulative = 0.00163211 +GAMG: Solving for p, Initial residual = 0.000116169, Final residual = 3.12311e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.44104e-06, global = 4.4403e-06, cumulative = 0.00163655 +smoothSolver: Solving for epsilon, Initial residual = 0.00156593, Final residual = 3.68953e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00258399, Final residual = 8.11357e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.104248 s +other Time = 0 s +rho Equations = 0.000178 s +U Equations = 0.00127 s +Y Equations = 0.00204727 s +E Equations = 0.000479 s +p Equations = 0.00176 s +calculate parcels = 70.7954 s +chemistry correctThermo = 0.002041 s +turbulence correct = 0.00081 s +combustion correct(in Y) = 0.0954617 s +percentage of chemistry = 91.5718 % +percentage of rho/U/Y/E = 3.81233 % +========Time details of each equation======= +rhoEqn Time = 0.000288 s +rhoEqn assamble = 0.000226 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001269 s +UEqn assamble = 0.000777 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000492 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001415 s +YEqn assamble = 0.000529 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.4e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000363 s +EEqn assamble = 0.000273 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 113.2 s ClockTime = 114 s +Courant Number mean: 0.00671734 max: 0.0319471 +Time = 0.00116 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 20829 + Current mass in system = 1.54918e-09 + Linear momentum = (3.15573e-11 -1.15876e-08 0) + |Linear momentum| = 1.15876e-08 + Linear kinetic energy = 4.51324e-08 + model1: + number of parcels added = 20859 + mass introduced = 1.62056e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.149, 540.2 + Mass transfer phase change = 7.13815e-11 + D10, D32, Dmax (mu) = 54.1731, 85.3341, 151.113 + Liquid penetration 95% mass (m) = 0.00836851 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00898774, Final residual = 1.23173e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.013778, Final residual = 8.10469e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00236775, Final residual = 3.39399e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00390975, Final residual = 5.28959e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00423886, Final residual = 6.22236e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00423908, Final residual = 6.23006e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00402168, Final residual = 3.30835e-07, No Iterations 1 +min/max(T) = 649.705, 2054.84 +GAMG: Solving for p, Initial residual = 0.0517267, Final residual = 0.000129296, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.88287e-06, global = 4.4598e-06, cumulative = 0.00164101 +GAMG: Solving for p, Initial residual = 0.000123458, Final residual = 2.46427e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.47834e-06, global = 4.47772e-06, cumulative = 0.00164548 +smoothSolver: Solving for epsilon, Initial residual = 0.00157418, Final residual = 3.7424e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00259477, Final residual = 8.23141e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.082497 s +other Time = 0 s +rho Equations = 0.000179 s +U Equations = 0.001252 s +Y Equations = 0.00207329 s +E Equations = 0.00049 s +p Equations = 0.00177 s +calculate parcels = 71.1318 s +chemistry correctThermo = 0.002028 s +turbulence correct = 0.000808 s +combustion correct(in Y) = 0.0737027 s +percentage of chemistry = 89.3399 % +percentage of rho/U/Y/E = 4.84174 % +========Time details of each equation======= +rhoEqn Time = 0.000289 s +rhoEqn assamble = 0.000228 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001251 s +UEqn assamble = 0.000749 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000502 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001435 s +YEqn assamble = 0.000534 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.5e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000369 s +EEqn assamble = 0.000276 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 113.62 s ClockTime = 114 s +Courant Number mean: 0.0068185 max: 0.0321125 +Time = 0.0011625 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 40 new parcels + +Cloud: sprayCloud + Current number of parcels = 20869 + Current mass in system = 1.5508e-09 + Linear momentum = (3.12685e-11 -1.15976e-08 0) + |Linear momentum| = 1.15976e-08 + Linear kinetic energy = 4.51562e-08 + model1: + number of parcels added = 20899 + mass introduced = 1.62258e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.165, 540.2 + Mass transfer phase change = 7.17734e-11 + D10, D32, Dmax (mu) = 54.1671, 85.3591, 151.128 + Liquid penetration 95% mass (m) = 0.00838692 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00872113, Final residual = 1.23286e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0136963, Final residual = 8.1523e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00236879, Final residual = 3.4258e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00391897, Final residual = 5.35122e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0042444, Final residual = 6.28731e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00424463, Final residual = 6.29514e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00405129, Final residual = 3.35647e-07, No Iterations 1 +min/max(T) = 650.194, 2065.69 +GAMG: Solving for p, Initial residual = 0.0522081, Final residual = 0.000133284, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.9515e-06, global = 4.50099e-06, cumulative = 0.00164998 +GAMG: Solving for p, Initial residual = 0.000126873, Final residual = 1.54878e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.51739e-06, global = 4.5169e-06, cumulative = 0.0016545 +smoothSolver: Solving for epsilon, Initial residual = 0.0015815, Final residual = 3.79624e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00260754, Final residual = 8.3611e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.1027 s +other Time = 0 s +rho Equations = 0.000173 s +U Equations = 0.001074 s +Y Equations = 0.00265548 s +E Equations = 0.000685 s +p Equations = 0.00259 s +calculate parcels = 71.4611 s +chemistry correctThermo = 0.003161 s +turbulence correct = 0.001125 s +combustion correct(in Y) = 0.0910085 s +percentage of chemistry = 88.6159 % +percentage of rho/U/Y/E = 4.46688 % +========Time details of each equation======= +rhoEqn Time = 0.000334 s +rhoEqn assamble = 0.000264 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001072 s +UEqn assamble = 0.000656 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000416 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002102 s +YEqn assamble = 0.000731 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000295 s +YEqn correct boundary = 0 s +EEqn Time = 0.000509 s +EEqn assamble = 0.000375 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000134 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 114.05 s ClockTime = 115 s +Courant Number mean: 0.00691946 max: 0.0322247 +Time = 0.001165 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 51 new parcels + +Cloud: sprayCloud + Current number of parcels = 20920 + Current mass in system = 1.55296e-09 + Linear momentum = (3.11242e-11 -1.16118e-08 0) + |Linear momentum| = 1.16119e-08 + Linear kinetic energy = 4.51967e-08 + model1: + number of parcels added = 20950 + mass introduced = 1.62513e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.158, 540.2 + Mass transfer phase change = 7.21691e-11 + D10, D32, Dmax (mu) = 54.1629, 85.3906, 151.144 + Liquid penetration 95% mass (m) = 0.00840226 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00820917, Final residual = 1.23429e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0136214, Final residual = 8.23348e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00236868, Final residual = 3.45761e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00393009, Final residual = 5.41665e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00425197, Final residual = 6.35049e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00425221, Final residual = 6.35829e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00407791, Final residual = 3.40135e-07, No Iterations 1 +min/max(T) = 650.722, 2076.57 +GAMG: Solving for p, Initial residual = 0.0527183, Final residual = 0.000120604, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.96125e-06, global = 4.54309e-06, cumulative = 0.00165904 +GAMG: Solving for p, Initial residual = 0.000114262, Final residual = 2.13541e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.56137e-06, global = 4.5607e-06, cumulative = 0.00166361 +smoothSolver: Solving for epsilon, Initial residual = 0.00158797, Final residual = 3.84912e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00262244, Final residual = 8.49957e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.098135 s +other Time = 1e-06 s +rho Equations = 0.000182 s +U Equations = 0.001274 s +Y Equations = 0.00243139 s +E Equations = 0.000609 s +p Equations = 0.001844 s +calculate parcels = 71.7919 s +chemistry correctThermo = 0.002344 s +turbulence correct = 0.00094 s +combustion correct(in Y) = 0.0882936 s +percentage of chemistry = 89.9716 % +percentage of rho/U/Y/E = 4.58184 % +========Time details of each equation======= +rhoEqn Time = 0.000305 s +rhoEqn assamble = 0.000238 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001274 s +UEqn assamble = 0.000774 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.0005 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00178 s +YEqn assamble = 0.000639 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000196 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 114.48 s ClockTime = 115 s +Courant Number mean: 0.00702038 max: 0.032228 +Time = 0.0011675 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 64 new parcels + +Cloud: sprayCloud + Current number of parcels = 20983 + Current mass in system = 1.55577e-09 + Linear momentum = (3.08198e-11 -1.16311e-08 0) + |Linear momentum| = 1.16312e-08 + Linear kinetic energy = 4.52571e-08 + model1: + number of parcels added = 21014 + mass introduced = 1.62834e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.162, 540.2 + Mass transfer phase change = 7.257e-11 + D10, D32, Dmax (mu) = 54.1912, 85.4104, 151.159 + Liquid penetration 95% mass (m) = 0.0084182 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00776489, Final residual = 1.2375e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0135765, Final residual = 8.36534e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00237553, Final residual = 3.49707e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00394201, Final residual = 5.48301e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00425949, Final residual = 6.4121e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00425973, Final residual = 6.41987e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00410648, Final residual = 3.44817e-07, No Iterations 1 +min/max(T) = 651.284, 2087.57 +GAMG: Solving for p, Initial residual = 0.0532462, Final residual = 0.000103094, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.96516e-06, global = 4.60406e-06, cumulative = 0.00166821 +GAMG: Solving for p, Initial residual = 9.7871e-05, Final residual = 1.83256e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.62147e-06, global = 4.62089e-06, cumulative = 0.00167283 +smoothSolver: Solving for epsilon, Initial residual = 0.00159347, Final residual = 3.89922e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00263793, Final residual = 8.64155e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103744 s +other Time = 0 s +rho Equations = 0.000212 s +U Equations = 0.001446 s +Y Equations = 0.00219518 s +E Equations = 0.000675 s +p Equations = 0.002897 s +calculate parcels = 72.1253 s +chemistry correctThermo = 0.00285 s +turbulence correct = 0.001216 s +combustion correct(in Y) = 0.0920168 s +percentage of chemistry = 88.696 % +percentage of rho/U/Y/E = 4.36476 % +========Time details of each equation======= +rhoEqn Time = 0.0004 s +rhoEqn assamble = 0.000307 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001446 s +UEqn assamble = 0.000883 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000563 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001529 s +YEqn assamble = 0.000583 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.4e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000548 s +EEqn assamble = 0.000399 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000149 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 114.92 s ClockTime = 115 s +Courant Number mean: 0.00712129 max: 0.0321593 +Time = 0.00117 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 60 new parcels + +Cloud: sprayCloud + Current number of parcels = 21043 + Current mass in system = 1.55839e-09 + Linear momentum = (3.06812e-11 -1.1649e-08 0) + |Linear momentum| = 1.1649e-08 + Linear kinetic energy = 4.53118e-08 + model1: + number of parcels added = 21074 + mass introduced = 1.63136e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.162, 540.2 + Mass transfer phase change = 7.29743e-11 + D10, D32, Dmax (mu) = 54.1876, 85.4333, 151.173 + Liquid penetration 95% mass (m) = 0.00843332 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00740137, Final residual = 1.23403e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0135302, Final residual = 8.49717e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00237682, Final residual = 3.51584e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00395182, Final residual = 5.5461e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00426566, Final residual = 6.46925e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00426591, Final residual = 6.47696e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00413445, Final residual = 3.4932e-07, No Iterations 1 +min/max(T) = 651.877, 2098.76 +GAMG: Solving for p, Initial residual = 0.0537795, Final residual = 9.44066e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.98405e-06, global = 4.64431e-06, cumulative = 0.00167747 +GAMG: Solving for p, Initial residual = 8.94366e-05, Final residual = 8.6292e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.66317e-06, global = 4.66024e-06, cumulative = 0.00168213 +smoothSolver: Solving for epsilon, Initial residual = 0.00159892, Final residual = 3.95132e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00265326, Final residual = 8.78819e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.078145 s +other Time = 1e-06 s +rho Equations = 0.000169 s +U Equations = 0.001152 s +Y Equations = 0.00216465 s +E Equations = 0.000497 s +p Equations = 0.00241 s +calculate parcels = 72.4363 s +chemistry correctThermo = 0.002923 s +turbulence correct = 0.000918 s +combustion correct(in Y) = 0.0676644 s +percentage of chemistry = 86.5882 % +percentage of rho/U/Y/E = 5.09648 % +========Time details of each equation======= +rhoEqn Time = 0.000328 s +rhoEqn assamble = 0.00026 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001151 s +UEqn assamble = 0.000697 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000454 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001562 s +YEqn assamble = 0.000543 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000114 s +YEqn correct boundary = 0 s +EEqn Time = 0.000376 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 115.31 s ClockTime = 116 s +Courant Number mean: 0.00722249 max: 0.032295 +Time = 0.0011725 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 54 new parcels + +Cloud: sprayCloud + Current number of parcels = 21097 + Current mass in system = 1.56071e-09 + Linear momentum = (3.10282e-11 -1.16646e-08 0) + |Linear momentum| = 1.16646e-08 + Linear kinetic energy = 4.53577e-08 + model1: + number of parcels added = 21128 + mass introduced = 1.63409e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.155, 540.2 + Mass transfer phase change = 7.33835e-11 + D10, D32, Dmax (mu) = 54.1818, 85.463, 151.188 + Liquid penetration 95% mass (m) = 0.00844961 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0071341, Final residual = 1.23528e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0134672, Final residual = 8.60989e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00239178, Final residual = 3.55862e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00396101, Final residual = 5.60661e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00427012, Final residual = 6.51606e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00427038, Final residual = 6.52387e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00416372, Final residual = 3.54479e-07, No Iterations 1 +min/max(T) = 652.504, 2110.18 +GAMG: Solving for p, Initial residual = 0.0543036, Final residual = 9.53723e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.04908e-06, global = 4.70268e-06, cumulative = 0.00168684 +GAMG: Solving for p, Initial residual = 9.23521e-05, Final residual = 8.18669e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.71886e-06, global = 4.71603e-06, cumulative = 0.00169155 +smoothSolver: Solving for epsilon, Initial residual = 0.00160407, Final residual = 4.00467e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00266803, Final residual = 8.93685e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.108433 s +other Time = 0 s +rho Equations = 0.00017 s +U Equations = 0.00127 s +Y Equations = 0.00258282 s +E Equations = 0.000607 s +p Equations = 0.00218 s +calculate parcels = 72.7234 s +chemistry correctThermo = 0.002819 s +turbulence correct = 0.001081 s +combustion correct(in Y) = 0.0975122 s +percentage of chemistry = 89.9285 % +percentage of rho/U/Y/E = 4.26975 % +========Time details of each equation======= +rhoEqn Time = 0.000322 s +rhoEqn assamble = 0.000255 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001268 s +UEqn assamble = 0.000705 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000563 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001789 s +YEqn assamble = 0.000729 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000105 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000338 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 115.71 s ClockTime = 116 s +Courant Number mean: 0.0073242 max: 0.0327331 +Time = 0.001175 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 21139 + Current mass in system = 1.56247e-09 + Linear momentum = (3.14501e-11 -1.1676e-08 0) + |Linear momentum| = 1.1676e-08 + Linear kinetic energy = 4.53878e-08 + model1: + number of parcels added = 21172 + mass introduced = 1.63632e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.161, 540.2 + Mass transfer phase change = 7.38458e-11 + D10, D32, Dmax (mu) = 54.3777, 85.4983, 151.203 + Liquid penetration 95% mass (m) = 0.00846627 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00695698, Final residual = 1.23363e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0133812, Final residual = 8.69091e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00261988, Final residual = 4.03389e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00398253, Final residual = 5.70243e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00425719, Final residual = 6.51741e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00425746, Final residual = 6.52534e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00424651, Final residual = 3.71639e-07, No Iterations 1 +min/max(T) = 653.174, 2121.83 +GAMG: Solving for p, Initial residual = 0.0551984, Final residual = 0.000273432, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.92078e-06, global = 5.16658e-06, cumulative = 0.00169672 +GAMG: Solving for p, Initial residual = 0.000254284, Final residual = 2.50603e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.32899e-06, global = 5.32854e-06, cumulative = 0.00170205 +smoothSolver: Solving for epsilon, Initial residual = 0.00160907, Final residual = 4.04057e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00268491, Final residual = 9.07155e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092238 s +other Time = 0 s +rho Equations = 0.000179 s +U Equations = 0.001251 s +Y Equations = 0.00212578 s +E Equations = 0.000498 s +p Equations = 0.001964 s +calculate parcels = 73.0635 s +chemistry correctThermo = 0.002058 s +turbulence correct = 0.000804 s +combustion correct(in Y) = 0.0831582 s +percentage of chemistry = 90.1561 % +percentage of rho/U/Y/E = 4.39491 % +========Time details of each equation======= +rhoEqn Time = 0.000299 s +rhoEqn assamble = 0.00024 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001249 s +UEqn assamble = 0.00075 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000499 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00146 s +YEqn assamble = 0.000542 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.2e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000374 s +EEqn assamble = 0.000281 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 116.14 s ClockTime = 117 s +Courant Number mean: 0.00742014 max: 0.0331112 +Time = 0.0011775 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 52 new parcels + +Cloud: sprayCloud + Current number of parcels = 21191 + Current mass in system = 1.56467e-09 + Linear momentum = (3.20682e-11 -1.16907e-08 0) + |Linear momentum| = 1.16908e-08 + Linear kinetic energy = 4.54301e-08 + model1: + number of parcels added = 21224 + mass introduced = 1.63894e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.147, 540.2 + Mass transfer phase change = 7.42651e-11 + D10, D32, Dmax (mu) = 54.2481, 85.4998, 151.219 + Liquid penetration 95% mass (m) = 0.00848334 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00804383, Final residual = 1.25504e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0134512, Final residual = 8.91971e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00242731, Final residual = 3.66803e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00396603, Final residual = 5.65675e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00426538, Final residual = 6.54825e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00426567, Final residual = 6.55662e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00423109, Final residual = 3.63857e-07, No Iterations 1 +min/max(T) = 653.896, 2134.21 +GAMG: Solving for p, Initial residual = 0.0555041, Final residual = 0.000346959, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.97843e-06, global = 4.71277e-06, cumulative = 0.00170676 +GAMG: Solving for p, Initial residual = 0.000324157, Final residual = 2.99573e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.83328e-06, global = 4.8322e-06, cumulative = 0.00171159 +smoothSolver: Solving for epsilon, Initial residual = 0.00160114, Final residual = 4.05545e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00267706, Final residual = 9.15742e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09113 s +other Time = 0 s +rho Equations = 0.000176 s +U Equations = 0.001199 s +Y Equations = 0.00246882 s +E Equations = 0.000603 s +p Equations = 0.002399 s +calculate parcels = 73.4023 s +chemistry correctThermo = 0.002826 s +turbulence correct = 0.00102 s +combustion correct(in Y) = 0.0802382 s +percentage of chemistry = 88.048 % +percentage of rho/U/Y/E = 4.87964 % +========Time details of each equation======= +rhoEqn Time = 0.000322 s +rhoEqn assamble = 0.000253 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001197 s +UEqn assamble = 0.000696 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000501 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001775 s +YEqn assamble = 0.000644 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000166 s +YEqn correct boundary = 0 s +EEqn Time = 0.000446 s +EEqn assamble = 0.000334 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 116.57 s ClockTime = 117 s +Courant Number mean: 0.00752189 max: 0.0334086 +Time = 0.00118 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 21238 + Current mass in system = 1.56667e-09 + Linear momentum = (3.2332e-11 -1.17038e-08 0) + |Linear momentum| = 1.17039e-08 + Linear kinetic energy = 4.54662e-08 + model1: + number of parcels added = 21272 + mass introduced = 1.64136e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.164, 540.2 + Mass transfer phase change = 7.46895e-11 + D10, D32, Dmax (mu) = 54.4041, 85.5234, 151.241 + Liquid penetration 95% mass (m) = 0.00850022 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00698463, Final residual = 1.17199e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0132194, Final residual = 8.74886e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0024445, Final residual = 3.71884e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00397709, Final residual = 5.76637e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00427185, Final residual = 6.65781e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00427212, Final residual = 6.66637e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00424246, Final residual = 3.68135e-07, No Iterations 1 +min/max(T) = 654.661, 2146.54 +GAMG: Solving for p, Initial residual = 0.0560054, Final residual = 0.000203619, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.6113e-06, global = 4.86591e-06, cumulative = 0.00171646 +GAMG: Solving for p, Initial residual = 0.000191443, Final residual = 7.3122e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.89445e-06, global = 4.89189e-06, cumulative = 0.00172135 +smoothSolver: Solving for epsilon, Initial residual = 0.00161537, Final residual = 4.14086e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00269466, Final residual = 9.31936e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103429 s +other Time = 1e-06 s +rho Equations = 0.000142 s +U Equations = 0.000962 s +Y Equations = 0.00260404 s +E Equations = 0.000725 s +p Equations = 0.002419 s +calculate parcels = 73.7441 s +chemistry correctThermo = 0.002355 s +turbulence correct = 0.000982 s +combustion correct(in Y) = 0.093025 s +percentage of chemistry = 89.9409 % +percentage of rho/U/Y/E = 4.28607 % +========Time details of each equation======= +rhoEqn Time = 0.000293 s +rhoEqn assamble = 0.000236 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000961 s +UEqn assamble = 0.000557 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000404 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002011 s +YEqn assamble = 0.000745 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000216 s +YEqn correct boundary = 0 s +EEqn Time = 0.000546 s +EEqn assamble = 0.000416 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00013 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 117.01 s ClockTime = 118 s +Courant Number mean: 0.00762705 max: 0.0337481 +Time = 0.0011825 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 21286 + Current mass in system = 1.56866e-09 + Linear momentum = (3.23962e-11 -1.17169e-08 0) + |Linear momentum| = 1.1717e-08 + Linear kinetic energy = 4.55022e-08 + model1: + number of parcels added = 21320 + mass introduced = 1.64377e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.146, 540.2 + Mass transfer phase change = 7.51169e-11 + D10, D32, Dmax (mu) = 53.9004, 85.522, 151.303 + Liquid penetration 95% mass (m) = 0.00851645 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00695323, Final residual = 1.21101e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0130393, Final residual = 8.59667e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00245051, Final residual = 3.73723e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00398552, Final residual = 5.84513e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00427576, Final residual = 6.73521e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00427603, Final residual = 6.74399e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00427304, Final residual = 3.75822e-07, No Iterations 1 +min/max(T) = 655.475, 2158.53 +GAMG: Solving for p, Initial residual = 0.0567122, Final residual = 0.000201384, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.57252e-06, global = 4.89361e-06, cumulative = 0.00172624 +GAMG: Solving for p, Initial residual = 0.000186629, Final residual = 4.99227e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.92808e-06, global = 4.92645e-06, cumulative = 0.00173117 +smoothSolver: Solving for epsilon, Initial residual = 0.00163089, Final residual = 4.24471e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00271488, Final residual = 9.50913e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.110517 s +other Time = 0 s +rho Equations = 0.000208 s +U Equations = 0.001141 s +Y Equations = 0.00278053 s +E Equations = 0.00067 s +p Equations = 0.00281 s +calculate parcels = 74.0988 s +chemistry correctThermo = 0.002957 s +turbulence correct = 0.001183 s +combustion correct(in Y) = 0.0985505 s +percentage of chemistry = 89.1722 % +percentage of rho/U/Y/E = 4.34279 % +========Time details of each equation======= +rhoEqn Time = 0.000389 s +rhoEqn assamble = 0.000315 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00114 s +UEqn assamble = 0.000715 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000425 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002217 s +YEqn assamble = 0.000783 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00026 s +YEqn correct boundary = 0 s +EEqn Time = 0.000496 s +EEqn assamble = 0.000378 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 117.48 s ClockTime = 118 s +Courant Number mean: 0.00773302 max: 0.034464 +Time = 0.001185 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 46 new parcels + +Cloud: sprayCloud + Current number of parcels = 21330 + Current mass in system = 1.57049e-09 + Linear momentum = (3.22101e-11 -1.17291e-08 0) + |Linear momentum| = 1.17291e-08 + Linear kinetic energy = 4.55352e-08 + model1: + number of parcels added = 21366 + mass introduced = 1.64608e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.172, 540.2 + Mass transfer phase change = 7.55904e-11 + D10, D32, Dmax (mu) = 54.0646, 85.5668, 151.367 + Liquid penetration 95% mass (m) = 0.00853472 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00719555, Final residual = 1.2488e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0128479, Final residual = 8.55797e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0026296, Final residual = 4.1935e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00399034, Final residual = 5.92202e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0042499, Final residual = 6.7398e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00425018, Final residual = 6.74797e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00434606, Final residual = 3.91566e-07, No Iterations 1 +min/max(T) = 656.335, 2170.62 +GAMG: Solving for p, Initial residual = 0.0574686, Final residual = 0.000308578, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.18143e-06, global = 5.31955e-06, cumulative = 0.00173649 +GAMG: Solving for p, Initial residual = 0.000291221, Final residual = 1.92821e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.45735e-06, global = 5.45689e-06, cumulative = 0.00174195 +smoothSolver: Solving for epsilon, Initial residual = 0.0016395, Final residual = 4.29976e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00273212, Final residual = 9.64692e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.081749 s +other Time = 0 s +rho Equations = 0.000174 s +U Equations = 0.00112 s +Y Equations = 0.00219032 s +E Equations = 0.000498 s +p Equations = 0.002124 s +calculate parcels = 74.3662 s +chemistry correctThermo = 0.002018 s +turbulence correct = 0.000914 s +combustion correct(in Y) = 0.0724977 s +percentage of chemistry = 88.6833 % +percentage of rho/U/Y/E = 4.8714 % +========Time details of each equation======= +rhoEqn Time = 0.000306 s +rhoEqn assamble = 0.000243 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001118 s +UEqn assamble = 0.000696 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000422 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001619 s +YEqn assamble = 0.000566 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000142 s +YEqn correct boundary = 0 s +EEqn Time = 0.000376 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 117.83 s ClockTime = 118 s +Courant Number mean: 0.00783442 max: 0.0357207 +Time = 0.0011875 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 39 new parcels + +Cloud: sprayCloud + Current number of parcels = 21368 + Current mass in system = 1.57201e-09 + Linear momentum = (3.19758e-11 -1.17388e-08 0) + |Linear momentum| = 1.17388e-08 + Linear kinetic energy = 4.55587e-08 + model1: + number of parcels added = 21405 + mass introduced = 1.64804e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.146, 540.2 + Mass transfer phase change = 7.60267e-11 + D10, D32, Dmax (mu) = 54.2113, 85.6, 151.432 + Liquid penetration 95% mass (m) = 0.00855299 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00767948, Final residual = 1.2527e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0128788, Final residual = 8.71226e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00244345, Final residual = 3.75137e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00393966, Final residual = 5.83057e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00421113, Final residual = 6.6859e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00421141, Final residual = 6.69393e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00433982, Final residual = 3.85227e-07, No Iterations 1 +min/max(T) = 657.234, 2188.43 +GAMG: Solving for p, Initial residual = 0.0576268, Final residual = 0.000359166, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.28403e-06, global = 4.93636e-06, cumulative = 0.00174688 +GAMG: Solving for p, Initial residual = 0.000335113, Final residual = 2.82075e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.0298e-06, global = 5.02886e-06, cumulative = 0.00175191 +smoothSolver: Solving for epsilon, Initial residual = 0.00164028, Final residual = 4.37217e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00272106, Final residual = 9.71778e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.08801 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001176 s +Y Equations = 0.00264347 s +E Equations = 0.000625 s +p Equations = 0.003046 s +calculate parcels = 74.7132 s +chemistry correctThermo = 0.002904 s +turbulence correct = 0.00106 s +combustion correct(in Y) = 0.0761665 s +percentage of chemistry = 86.543 % +percentage of rho/U/Y/E = 5.25108 % +========Time details of each equation======= +rhoEqn Time = 0.000372 s +rhoEqn assamble = 0.000293 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001175 s +UEqn assamble = 0.000726 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000449 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001816 s +YEqn assamble = 0.000694 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000104 s +YEqn correct boundary = 0 s +EEqn Time = 0.000458 s +EEqn assamble = 0.000345 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 118.26 s ClockTime = 119 s +Courant Number mean: 0.00793942 max: 0.0368297 +Time = 0.00119 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 59 new parcels + +Cloud: sprayCloud + Current number of parcels = 21425 + Current mass in system = 1.57451e-09 + Linear momentum = (3.13607e-11 -1.17561e-08 0) + |Linear momentum| = 1.17562e-08 + Linear kinetic energy = 4.56123e-08 + model1: + number of parcels added = 21464 + mass introduced = 1.65098e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.172, 540.2 + Mass transfer phase change = 7.64671e-11 + D10, D32, Dmax (mu) = 54.5159, 85.6338, 151.499 + Liquid penetration 95% mass (m) = 0.00856984 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00701847, Final residual = 1.1943e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0127441, Final residual = 8.61327e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0024338, Final residual = 3.71151e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0039121, Final residual = 5.79415e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00417261, Final residual = 6.62447e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00417289, Final residual = 6.63216e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00436517, Final residual = 3.88754e-07, No Iterations 1 +min/max(T) = 658.162, 2207.42 +GAMG: Solving for p, Initial residual = 0.057532, Final residual = 0.000233316, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.83184e-06, global = 5.02005e-06, cumulative = 0.00175693 +GAMG: Solving for p, Initial residual = 0.000220338, Final residual = 7.78619e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.07851e-06, global = 5.07608e-06, cumulative = 0.00176201 +smoothSolver: Solving for epsilon, Initial residual = 0.00165635, Final residual = 4.50566e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00272448, Final residual = 9.8401e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095415 s +other Time = 1e-06 s +rho Equations = 0.000251 s +U Equations = 0.001078 s +Y Equations = 0.00268166 s +E Equations = 0.000705 s +p Equations = 0.002752 s +calculate parcels = 75.0706 s +chemistry correctThermo = 0.002984 s +turbulence correct = 0.001153 s +combustion correct(in Y) = 0.0835483 s +percentage of chemistry = 87.5631 % +percentage of rho/U/Y/E = 4.94226 % +========Time details of each equation======= +rhoEqn Time = 0.000435 s +rhoEqn assamble = 0.000336 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001077 s +UEqn assamble = 0.000638 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000439 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002109 s +YEqn assamble = 0.000749 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000269 s +YEqn correct boundary = 0 s +EEqn Time = 0.000528 s +EEqn assamble = 0.000389 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000139 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 118.72 s ClockTime = 119 s +Courant Number mean: 0.0080449 max: 0.0373144 +Time = 0.0011925 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 21472 + Current mass in system = 1.57647e-09 + Linear momentum = (3.14056e-11 -1.17696e-08 0) + |Linear momentum| = 1.17696e-08 + Linear kinetic energy = 4.56511e-08 + model1: + number of parcels added = 21513 + mass introduced = 1.65342e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.146, 540.2 + Mass transfer phase change = 7.69572e-11 + D10, D32, Dmax (mu) = 54.6587, 85.6754, 151.567 + Liquid penetration 95% mass (m) = 0.00858632 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00641157, Final residual = 1.12758e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.012607, Final residual = 8.60917e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00264966, Final residual = 4.04507e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00390445, Final residual = 5.73864e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00413112, Final residual = 6.51996e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00413143, Final residual = 6.52739e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00444136, Final residual = 3.99447e-07, No Iterations 1 +min/max(T) = 659.124, 2225.75 +GAMG: Solving for p, Initial residual = 0.0583641, Final residual = 0.00042809, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.62327e-06, global = 5.39664e-06, cumulative = 0.00176741 +GAMG: Solving for p, Initial residual = 0.000403843, Final residual = 3.26067e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.64937e-06, global = 5.64859e-06, cumulative = 0.00177305 +smoothSolver: Solving for epsilon, Initial residual = 0.00167347, Final residual = 4.57332e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00272678, Final residual = 9.89066e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.104272 s +other Time = 0 s +rho Equations = 0.000183 s +U Equations = 0.001206 s +Y Equations = 0.00262671 s +E Equations = 0.000625 s +p Equations = 0.002443 s +calculate parcels = 75.43 s +chemistry correctThermo = 0.002816 s +turbulence correct = 0.000965 s +combustion correct(in Y) = 0.0932033 s +percentage of chemistry = 89.3848 % +percentage of rho/U/Y/E = 4.45058 % +========Time details of each equation======= +rhoEqn Time = 0.000335 s +rhoEqn assamble = 0.000265 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001205 s +UEqn assamble = 0.0007 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000505 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001994 s +YEqn assamble = 0.000725 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00026 s +YEqn correct boundary = 0 s +EEqn Time = 0.000464 s +EEqn assamble = 0.000345 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000119 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 119.18 s ClockTime = 120 s +Courant Number mean: 0.00813934 max: 0.0375937 +Time = 0.001195 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 58 new parcels + +Cloud: sprayCloud + Current number of parcels = 21530 + Current mass in system = 1.57892e-09 + Linear momentum = (3.12179e-11 -1.17865e-08 0) + |Linear momentum| = 1.17866e-08 + Linear kinetic energy = 4.57036e-08 + model1: + number of parcels added = 21571 + mass introduced = 1.65632e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.154, 540.2 + Mass transfer phase change = 7.74015e-11 + D10, D32, Dmax (mu) = 54.6375, 85.7057, 151.638 + Liquid penetration 95% mass (m) = 0.00860343 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00645923, Final residual = 9.75341e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0125041, Final residual = 8.53226e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00240693, Final residual = 3.61353e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0038737, Final residual = 5.71255e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00412258, Final residual = 6.48593e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0041229, Final residual = 6.49313e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00440533, Final residual = 3.99304e-07, No Iterations 1 +min/max(T) = 660.127, 2243.77 +GAMG: Solving for p, Initial residual = 0.0588842, Final residual = 0.000447392, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.51377e-06, global = 5.00227e-06, cumulative = 0.00177806 +GAMG: Solving for p, Initial residual = 0.000413998, Final residual = 2.54959e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.12261e-06, global = 5.12175e-06, cumulative = 0.00178318 +smoothSolver: Solving for epsilon, Initial residual = 0.00165023, Final residual = 4.55666e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00269629, Final residual = 9.8676e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.115262 s +other Time = 0 s +rho Equations = 0.000182 s +U Equations = 0.001538 s +Y Equations = 0.00270344 s +E Equations = 0.000641 s +p Equations = 0.00303 s +calculate parcels = 75.7794 s +chemistry correctThermo = 0.002875 s +turbulence correct = 0.001302 s +combustion correct(in Y) = 0.102755 s +percentage of chemistry = 89.1487 % +percentage of rho/U/Y/E = 4.39385 % +========Time details of each equation======= +rhoEqn Time = 0.000392 s +rhoEqn assamble = 0.000312 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001537 s +UEqn assamble = 0.000948 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000589 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001977 s +YEqn assamble = 0.000735 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000199 s +YEqn correct boundary = 0 s +EEqn Time = 0.000486 s +EEqn assamble = 0.000355 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000131 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 119.64 s ClockTime = 120 s +Courant Number mean: 0.00823501 max: 0.0375821 +Time = 0.0011975 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 21575 + Current mass in system = 1.58083e-09 + Linear momentum = (3.04716e-11 -1.17995e-08 0) + |Linear momentum| = 1.17995e-08 + Linear kinetic energy = 4.57407e-08 + model1: + number of parcels added = 21619 + mass introduced = 1.65872e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.148, 540.2 + Mass transfer phase change = 7.78924e-11 + D10, D32, Dmax (mu) = 54.9689, 85.735, 151.709 + Liquid penetration 95% mass (m) = 0.00862072 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00606008, Final residual = 8.93197e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.012219, Final residual = 8.34154e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00259057, Final residual = 4.11554e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00388553, Final residual = 5.77522e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00410947, Final residual = 6.45091e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00410977, Final residual = 6.45806e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00442654, Final residual = 4.09974e-07, No Iterations 1 +min/max(T) = 661.192, 2261.79 +GAMG: Solving for p, Initial residual = 0.0593855, Final residual = 0.000313965, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.46518e-06, global = 5.58299e-06, cumulative = 0.00178876 +GAMG: Solving for p, Initial residual = 0.000294847, Final residual = 9.51393e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.66018e-06, global = 5.65823e-06, cumulative = 0.00179442 +smoothSolver: Solving for epsilon, Initial residual = 0.00165465, Final residual = 4.55004e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00269578, Final residual = 9.89142e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.077329 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001211 s +Y Equations = 0.00274776 s +E Equations = 0.000563 s +p Equations = 0.002297 s +calculate parcels = 76.1264 s +chemistry correctThermo = 0.00195 s +turbulence correct = 0.000962 s +combustion correct(in Y) = 0.0672142 s +percentage of chemistry = 86.9198 % +percentage of rho/U/Y/E = 6.07633 % +========Time details of each equation======= +rhoEqn Time = 0.000331 s +rhoEqn assamble = 0.000267 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00121 s +UEqn assamble = 0.000768 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000442 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002131 s +YEqn assamble = 0.000676 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000199 s +YEqn correct boundary = 0 s +EEqn Time = 0.000425 s +EEqn assamble = 0.000326 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 120.07 s ClockTime = 121 s +Courant Number mean: 0.00832568 max: 0.0374937 +Time = 0.0012 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 55 new parcels + +Cloud: sprayCloud + Current number of parcels = 21628 + Current mass in system = 1.58304e-09 + Linear momentum = (3.02006e-11 -1.18149e-08 0) + |Linear momentum| = 1.18149e-08 + Linear kinetic energy = 4.57873e-08 + model1: + number of parcels added = 21674 + mass introduced = 1.66146e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.16, 540.2 + Mass transfer phase change = 7.84188e-11 + D10, D32, Dmax (mu) = 54.9614, 85.7589, 151.781 + Liquid penetration 95% mass (m) = 0.00863697 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00700555, Final residual = 1.00699e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.012141, Final residual = 8.49814e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00272046, Final residual = 4.30741e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00388027, Final residual = 5.71531e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00408417, Final residual = 6.39899e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00408449, Final residual = 6.40613e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00445672, Final residual = 4.1315e-07, No Iterations 1 +min/max(T) = 662.306, 2279.81 +GAMG: Solving for p, Initial residual = 0.0607027, Final residual = 0.000428446, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.26472e-06, global = 5.84969e-06, cumulative = 0.00180027 +GAMG: Solving for p, Initial residual = 0.000391637, Final residual = 3.89284e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.06752e-06, global = 6.0663e-06, cumulative = 0.00180634 +smoothSolver: Solving for epsilon, Initial residual = 0.00165658, Final residual = 4.54419e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00269316, Final residual = 9.9127e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103462 s +other Time = 1e-06 s +rho Equations = 0.000173 s +U Equations = 0.001264 s +Y Equations = 0.0025046 s +E Equations = 0.000669 s +p Equations = 0.002817 s +calculate parcels = 76.4221 s +chemistry correctThermo = 0.002874 s +turbulence correct = 0.001176 s +combustion correct(in Y) = 0.0917214 s +percentage of chemistry = 88.6523 % +percentage of rho/U/Y/E = 4.45632 % +========Time details of each equation======= +rhoEqn Time = 0.000347 s +rhoEqn assamble = 0.000274 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001264 s +UEqn assamble = 0.000771 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000493 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001872 s +YEqn assamble = 0.000671 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000185 s +YEqn correct boundary = 0 s +EEqn Time = 0.000486 s +EEqn assamble = 0.000365 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000121 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 120.82 s ClockTime = 121 s +Courant Number mean: 0.00841018 max: 0.0372677 +Time = 0.0012025 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 48 new parcels + +Cloud: sprayCloud + Current number of parcels = 21675 + Current mass in system = 1.58495e-09 + Linear momentum = (2.99103e-11 -1.18277e-08 0) + |Linear momentum| = 1.18277e-08 + Linear kinetic energy = 4.58231e-08 + model1: + number of parcels added = 21722 + mass introduced = 1.66386e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.168, 540.2 + Mass transfer phase change = 7.89163e-11 + D10, D32, Dmax (mu) = 54.9553, 85.7792, 151.838 + Liquid penetration 95% mass (m) = 0.00865247 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00811585, Final residual = 1.03888e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0121147, Final residual = 8.73274e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00258767, Final residual = 4.04499e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00384681, Final residual = 5.70113e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00406325, Final residual = 6.38722e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00406359, Final residual = 6.39433e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00441818, Final residual = 4.05951e-07, No Iterations 1 +min/max(T) = 663.468, 2297.71 +GAMG: Solving for p, Initial residual = 0.0609471, Final residual = 0.000369146, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.02975e-06, global = 5.6202e-06, cumulative = 0.00181196 +GAMG: Solving for p, Initial residual = 0.000347606, Final residual = 2.87585e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.73546e-06, global = 5.73445e-06, cumulative = 0.00181769 +smoothSolver: Solving for epsilon, Initial residual = 0.00163512, Final residual = 4.50501e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.002671, Final residual = 9.89938e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094322 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001316 s +Y Equations = 0.00264457 s +E Equations = 0.000683 s +p Equations = 0.002698 s +calculate parcels = 76.7952 s +chemistry correctThermo = 0.002815 s +turbulence correct = 0.001119 s +combustion correct(in Y) = 0.0826664 s +percentage of chemistry = 87.6428 % +percentage of rho/U/Y/E = 5.11076 % +========Time details of each equation======= +rhoEqn Time = 0.000344 s +rhoEqn assamble = 0.000261 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001315 s +UEqn assamble = 0.000813 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000502 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002008 s +YEqn assamble = 0.000721 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00021 s +YEqn correct boundary = 0 s +EEqn Time = 0.000496 s +EEqn assamble = 0.000351 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000145 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 121.29 s ClockTime = 122 s +Courant Number mean: 0.00849886 max: 0.0370189 +Time = 0.001205 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 21723 + Current mass in system = 1.58694e-09 + Linear momentum = (2.99042e-11 -1.1841e-08 0) + |Linear momentum| = 1.1841e-08 + Linear kinetic energy = 4.58604e-08 + model1: + number of parcels added = 21772 + mass introduced = 1.66636e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.156, 540.2 + Mass transfer phase change = 7.94154e-11 + D10, D32, Dmax (mu) = 55.0845, 85.814, 151.892 + Liquid penetration 95% mass (m) = 0.00867044 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00727228, Final residual = 1.0385e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0118926, Final residual = 8.68788e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00255927, Final residual = 3.96137e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00383485, Final residual = 5.67058e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00404804, Final residual = 6.35422e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00404836, Final residual = 6.36171e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00440751, Final residual = 4.05315e-07, No Iterations 1 +min/max(T) = 664.679, 2315.38 +GAMG: Solving for p, Initial residual = 0.0613704, Final residual = 0.000285832, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.76344e-06, global = 5.71033e-06, cumulative = 0.0018234 +GAMG: Solving for p, Initial residual = 0.000269729, Final residual = 6.36283e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.75454e-06, global = 5.7524e-06, cumulative = 0.00182915 +smoothSolver: Solving for epsilon, Initial residual = 0.0016307, Final residual = 4.51176e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00266669, Final residual = 9.94438e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103538 s +other Time = 0 s +rho Equations = 0.000184 s +U Equations = 0.00126 s +Y Equations = 0.00244272 s +E Equations = 0.000611 s +p Equations = 0.002253 s +calculate parcels = 77.1142 s +chemistry correctThermo = 0.00287 s +turbulence correct = 0.00107 s +combustion correct(in Y) = 0.0926373 s +percentage of chemistry = 89.4718 % +percentage of rho/U/Y/E = 4.34403 % +========Time details of each equation======= +rhoEqn Time = 0.000333 s +rhoEqn assamble = 0.000265 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00126 s +UEqn assamble = 0.000771 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000489 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001801 s +YEqn assamble = 0.000652 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000182 s +YEqn correct boundary = 0 s +EEqn Time = 0.000454 s +EEqn assamble = 0.000331 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000123 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 121.71 s ClockTime = 122 s +Courant Number mean: 0.00859159 max: 0.0368316 +Time = 0.0012075 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 39 new parcels + +Cloud: sprayCloud + Current number of parcels = 21762 + Current mass in system = 1.58843e-09 + Linear momentum = (2.97665e-11 -1.18501e-08 0) + |Linear momentum| = 1.18502e-08 + Linear kinetic energy = 4.58811e-08 + model1: + number of parcels added = 21811 + mass introduced = 1.6683e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.15, 540.2 + Mass transfer phase change = 7.98728e-11 + D10, D32, Dmax (mu) = 55.0214, 85.8266, 151.949 + Liquid penetration 95% mass (m) = 0.00868896 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00633958, Final residual = 1.09023e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0116726, Final residual = 8.53371e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0023787, Final residual = 3.64132e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00381833, Final residual = 5.6274e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00404894, Final residual = 6.34117e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00404927, Final residual = 6.34835e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00437629, Final residual = 4.00538e-07, No Iterations 1 +min/max(T) = 665.942, 2332.67 +GAMG: Solving for p, Initial residual = 0.0626068, Final residual = 0.000385422, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.64333e-06, global = 5.17331e-06, cumulative = 0.00183433 +GAMG: Solving for p, Initial residual = 0.000363949, Final residual = 9.62969e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.2763e-06, global = 5.27314e-06, cumulative = 0.0018396 +smoothSolver: Solving for epsilon, Initial residual = 0.00163352, Final residual = 4.57944e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00267048, Final residual = 4.76151e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.106338 s +other Time = 0 s +rho Equations = 0.000178 s +U Equations = 0.001238 s +Y Equations = 0.00241689 s +E Equations = 0.000602 s +p Equations = 0.002327 s +calculate parcels = 77.4787 s +chemistry correctThermo = 0.00282 s +turbulence correct = 0.001196 s +combustion correct(in Y) = 0.0953601 s +percentage of chemistry = 89.6764 % +percentage of rho/U/Y/E = 4.17056 % +========Time details of each equation======= +rhoEqn Time = 0.000319 s +rhoEqn assamble = 0.000253 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001236 s +UEqn assamble = 0.000724 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000512 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001756 s +YEqn assamble = 0.000631 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000186 s +YEqn correct boundary = 0 s +EEqn Time = 0.000441 s +EEqn assamble = 0.000329 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 122.18 s ClockTime = 123 s +Courant Number mean: 0.00869191 max: 0.0369859 +Time = 0.00121 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 21811 + Current mass in system = 1.59039e-09 + Linear momentum = (3.00595e-11 -1.18627e-08 0) + |Linear momentum| = 1.18628e-08 + Linear kinetic energy = 4.59147e-08 + model1: + number of parcels added = 21860 + mass introduced = 1.67072e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.153, 540.2 + Mass transfer phase change = 8.03332e-11 + D10, D32, Dmax (mu) = 55.0075, 85.8585, 152.008 + Liquid penetration 95% mass (m) = 0.00870713 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00721591, Final residual = 1.36534e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0114878, Final residual = 8.32333e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00237141, Final residual = 3.62036e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00382137, Final residual = 5.64949e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00404758, Final residual = 6.35122e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00404791, Final residual = 6.35827e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00438745, Final residual = 4.04045e-07, No Iterations 1 +min/max(T) = 667.255, 2349.41 +GAMG: Solving for p, Initial residual = 0.0639752, Final residual = 0.000354426, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.44123e-06, global = 5.25203e-06, cumulative = 0.00184485 +GAMG: Solving for p, Initial residual = 0.000333886, Final residual = 8.5245e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.30854e-06, global = 5.30652e-06, cumulative = 0.00185016 +smoothSolver: Solving for epsilon, Initial residual = 0.00165178, Final residual = 4.6694e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00269023, Final residual = 4.8847e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.085327 s +other Time = 0 s +rho Equations = 0.000167 s +U Equations = 0.001225 s +Y Equations = 0.00211661 s +E Equations = 0.000499 s +p Equations = 0.001833 s +calculate parcels = 77.7868 s +chemistry correctThermo = 0.001959 s +turbulence correct = 0.000882 s +combustion correct(in Y) = 0.0764494 s +percentage of chemistry = 89.5958 % +percentage of rho/U/Y/E = 4.69677 % +========Time details of each equation======= +rhoEqn Time = 0.000286 s +rhoEqn assamble = 0.000228 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001224 s +UEqn assamble = 0.000776 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000448 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001548 s +YEqn assamble = 0.000552 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000127 s +YEqn correct boundary = 0 s +EEqn Time = 0.000374 s +EEqn assamble = 0.000279 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 122.58 s ClockTime = 123 s +Courant Number mean: 0.00879546 max: 0.0373821 +Time = 0.0012125 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 44 new parcels + +Cloud: sprayCloud + Current number of parcels = 21851 + Current mass in system = 1.59198e-09 + Linear momentum = (3.01503e-11 -1.18726e-08 0) + |Linear momentum| = 1.18726e-08 + Linear kinetic energy = 4.59375e-08 + model1: + number of parcels added = 21904 + mass introduced = 1.67286e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.151, 540.2 + Mass transfer phase change = 8.08794e-11 + D10, D32, Dmax (mu) = 55.2351, 85.9017, 152.068 + Liquid penetration 95% mass (m) = 0.00872598 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00845741, Final residual = 1.56061e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0111816, Final residual = 8.0747e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00270101, Final residual = 4.42093e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00383119, Final residual = 5.68254e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00401437, Final residual = 6.32648e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00401471, Final residual = 6.33317e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0044862, Final residual = 4.28356e-07, No Iterations 1 +min/max(T) = 668.63, 2365.51 +GAMG: Solving for p, Initial residual = 0.0655238, Final residual = 0.000594014, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.54714e-06, global = 5.91825e-06, cumulative = 0.00185608 +GAMG: Solving for p, Initial residual = 0.000554139, Final residual = 5.27028e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.29603e-06, global = 6.2948e-06, cumulative = 0.00186237 +smoothSolver: Solving for epsilon, Initial residual = 0.00166092, Final residual = 4.63625e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00269728, Final residual = 4.94723e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.10886 s +other Time = 1e-06 s +rho Equations = 0.000154 s +U Equations = 0.001022 s +Y Equations = 0.0023977 s +E Equations = 0.000663 s +p Equations = 0.002376 s +calculate parcels = 78.1125 s +chemistry correctThermo = 0.002843 s +turbulence correct = 0.00112 s +combustion correct(in Y) = 0.0981083 s +percentage of chemistry = 90.1234 % +percentage of rho/U/Y/E = 3.89188 % +========Time details of each equation======= +rhoEqn Time = 0.00029 s +rhoEqn assamble = 0.000231 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00102 s +UEqn assamble = 0.000616 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000404 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001866 s +YEqn assamble = 0.000624 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000236 s +YEqn correct boundary = 0 s +EEqn Time = 0.000508 s +EEqn assamble = 0.000334 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000174 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 123.01 s ClockTime = 124 s +Courant Number mean: 0.00888691 max: 0.0374041 +Time = 0.001215 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 67 new parcels + +Cloud: sprayCloud + Current number of parcels = 21915 + Current mass in system = 1.5947e-09 + Linear momentum = (2.96565e-11 -1.18903e-08 0) + |Linear momentum| = 1.18903e-08 + Linear kinetic energy = 4.59881e-08 + model1: + number of parcels added = 21971 + mass introduced = 1.67607e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.156, 540.2 + Mass transfer phase change = 8.13749e-11 + D10, D32, Dmax (mu) = 55.5895, 85.9366, 152.13 + Liquid penetration 95% mass (m) = 0.00874333 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0106058, Final residual = 1.78938e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0111686, Final residual = 8.26751e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00248088, Final residual = 3.97218e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00377749, Final residual = 5.63204e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00398081, Final residual = 6.26543e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00398115, Final residual = 6.27186e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00445806, Final residual = 4.21039e-07, No Iterations 1 +min/max(T) = 670.063, 2381.16 +GAMG: Solving for p, Initial residual = 0.0668806, Final residual = 0.000546032, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.54231e-06, global = 5.75649e-06, cumulative = 0.00186813 +GAMG: Solving for p, Initial residual = 0.00051587, Final residual = 3.7246e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.71247e-06, global = 5.71121e-06, cumulative = 0.00187384 +smoothSolver: Solving for epsilon, Initial residual = 0.00161124, Final residual = 4.5332e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00264984, Final residual = 4.94575e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.097653 s +other Time = 1e-06 s +rho Equations = 0.000149 s +U Equations = 0.000985 s +Y Equations = 0.00270012 s +E Equations = 0.000664 s +p Equations = 0.002633 s +calculate parcels = 78.464 s +chemistry correctThermo = 0.002998 s +turbulence correct = 0.001304 s +combustion correct(in Y) = 0.0860379 s +percentage of chemistry = 88.1057 % +percentage of rho/U/Y/E = 4.60623 % +========Time details of each equation======= +rhoEqn Time = 0.000311 s +rhoEqn assamble = 0.000249 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000983 s +UEqn assamble = 0.000575 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000408 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002143 s +YEqn assamble = 0.000781 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000266 s +YEqn correct boundary = 0 s +EEqn Time = 0.000501 s +EEqn assamble = 0.000372 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000129 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 123.46 s ClockTime = 124 s +Courant Number mean: 0.00898426 max: 0.0369287 +Time = 0.0012175 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 41 new parcels + +Cloud: sprayCloud + Current number of parcels = 21956 + Current mass in system = 1.59618e-09 + Linear momentum = (2.96144e-11 -1.18986e-08 0) + |Linear momentum| = 1.18986e-08 + Linear kinetic energy = 4.60028e-08 + model1: + number of parcels added = 22012 + mass introduced = 1.67802e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.144, 540.2 + Mass transfer phase change = 8.18407e-11 + D10, D32, Dmax (mu) = 55.5463, 85.9511, 152.192 + Liquid penetration 95% mass (m) = 0.00876189 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00992138, Final residual = 1.671e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0108912, Final residual = 8.1333e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00233456, Final residual = 3.54609e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00374416, Final residual = 5.56117e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00395464, Final residual = 6.216e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00395498, Final residual = 6.22205e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00443205, Final residual = 4.14591e-07, No Iterations 1 +min/max(T) = 671.53, 2396.6 +GAMG: Solving for p, Initial residual = 0.0667247, Final residual = 0.000435486, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.7804e-06, global = 5.24469e-06, cumulative = 0.00187908 +GAMG: Solving for p, Initial residual = 0.000406875, Final residual = 3.31902e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.37049e-06, global = 5.36939e-06, cumulative = 0.00188445 +smoothSolver: Solving for epsilon, Initial residual = 0.00161477, Final residual = 4.60091e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00264319, Final residual = 5.02018e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.099462 s +other Time = 1e-06 s +rho Equations = 0.000178 s +U Equations = 0.001292 s +Y Equations = 0.00218136 s +E Equations = 0.000491 s +p Equations = 0.002019 s +calculate parcels = 78.8306 s +chemistry correctThermo = 0.00203 s +turbulence correct = 0.000957 s +combustion correct(in Y) = 0.0901106 s +percentage of chemistry = 90.5981 % +percentage of rho/U/Y/E = 4.16476 % +========Time details of each equation======= +rhoEqn Time = 0.000297 s +rhoEqn assamble = 0.000238 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001292 s +UEqn assamble = 0.000794 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000498 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001474 s +YEqn assamble = 0.000538 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 7.8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.00037 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 123.93 s ClockTime = 124 s +Courant Number mean: 0.00908716 max: 0.0368306 +Time = 0.00122 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 22003 + Current mass in system = 1.59794e-09 + Linear momentum = (2.96881e-11 -1.19087e-08 0) + |Linear momentum| = 1.19088e-08 + Linear kinetic energy = 4.60236e-08 + model1: + number of parcels added = 22061 + mass introduced = 1.6803e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.142, 540.2 + Mass transfer phase change = 8.23566e-11 + D10, D32, Dmax (mu) = 55.81, 85.9975, 152.257 + Liquid penetration 95% mass (m) = 0.00877882 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00895458, Final residual = 1.6239e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0105677, Final residual = 7.8893e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00255874, Final residual = 4.22951e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00373431, Final residual = 5.59078e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00391682, Final residual = 6.13749e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00391717, Final residual = 6.1435e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00449418, Final residual = 4.30237e-07, No Iterations 1 +min/max(T) = 673.042, 2411.39 +GAMG: Solving for p, Initial residual = 0.0682839, Final residual = 0.000458358, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.86655e-06, global = 5.74946e-06, cumulative = 0.0018902 +GAMG: Solving for p, Initial residual = 0.000427887, Final residual = 3.28213e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.94604e-06, global = 5.94548e-06, cumulative = 0.00189615 +smoothSolver: Solving for epsilon, Initial residual = 0.0016302, Final residual = 4.66382e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00265254, Final residual = 5.08943e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.10697 s +other Time = 1e-06 s +rho Equations = 0.000235 s +U Equations = 0.001768 s +Y Equations = 0.00247394 s +E Equations = 0.000502 s +p Equations = 0.002122 s +calculate parcels = 79.2012 s +chemistry correctThermo = 0.002038 s +turbulence correct = 0.000883 s +combustion correct(in Y) = 0.0967091 s +percentage of chemistry = 90.4077 % +percentage of rho/U/Y/E = 4.65452 % +========Time details of each equation======= +rhoEqn Time = 0.000366 s +rhoEqn assamble = 0.000278 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001766 s +UEqn assamble = 0.000984 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000782 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001397 s +YEqn assamble = 0.000601 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -0.000115 s +YEqn correct boundary = 0 s +EEqn Time = 0.000382 s +EEqn assamble = 0.000286 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 124.41 s ClockTime = 125 s +Courant Number mean: 0.00917971 max: 0.0370319 +Time = 0.0012225 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 50 new parcels + +Cloud: sprayCloud + Current number of parcels = 22048 + Current mass in system = 1.59967e-09 + Linear momentum = (2.97586e-11 -1.19183e-08 0) + |Linear momentum| = 1.19183e-08 + Linear kinetic energy = 4.60413e-08 + model1: + number of parcels added = 22111 + mass introduced = 1.68259e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.148, 540.2 + Mass transfer phase change = 8.29261e-11 + D10, D32, Dmax (mu) = 56.2059, 86.0468, 152.321 + Liquid penetration 95% mass (m) = 0.00879808 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00802988, Final residual = 1.49206e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0103642, Final residual = 7.79608e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00270586, Final residual = 4.4103e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00370223, Final residual = 5.48878e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00385643, Final residual = 6.04447e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00385679, Final residual = 6.05049e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00455205, Final residual = 4.39164e-07, No Iterations 1 +min/max(T) = 674.62, 2425.38 +GAMG: Solving for p, Initial residual = 0.0691428, Final residual = 0.000473754, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.60301e-06, global = 6.1729e-06, cumulative = 0.00190232 +GAMG: Solving for p, Initial residual = 0.00044917, Final residual = 3.23224e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.56544e-06, global = 6.56465e-06, cumulative = 0.00190889 +smoothSolver: Solving for epsilon, Initial residual = 0.00161022, Final residual = 4.57912e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00263096, Final residual = 5.0573e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.074991 s +other Time = 1e-06 s +rho Equations = 0.00018 s +U Equations = 0.001086 s +Y Equations = 0.00239215 s +E Equations = 0.000512 s +p Equations = 0.002056 s +calculate parcels = 79.5906 s +chemistry correctThermo = 0.001946 s +turbulence correct = 0.000928 s +combustion correct(in Y) = 0.0656979 s +percentage of chemistry = 87.6077 % +percentage of rho/U/Y/E = 5.56086 % +========Time details of each equation======= +rhoEqn Time = 0.000307 s +rhoEqn assamble = 0.000246 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001084 s +UEqn assamble = 0.000645 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000439 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001795 s +YEqn assamble = 0.000572 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000251 s +YEqn correct boundary = 0 s +EEqn Time = 0.000384 s +EEqn assamble = 0.000292 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 124.87 s ClockTime = 125 s +Courant Number mean: 0.00925649 max: 0.0375691 +Time = 0.001225 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 22095 + Current mass in system = 1.6014e-09 + Linear momentum = (3.01313e-11 -1.19274e-08 0) + |Linear momentum| = 1.19274e-08 + Linear kinetic energy = 4.60554e-08 + model1: + number of parcels added = 22160 + mass introduced = 1.6848e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.143, 540.2 + Mass transfer phase change = 8.34065e-11 + D10, D32, Dmax (mu) = 56.46, 86.0838, 152.385 + Liquid penetration 95% mass (m) = 0.00881542 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00846275, Final residual = 1.37222e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0103753, Final residual = 7.92076e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00233461, Final residual = 3.59261e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00361863, Final residual = 5.35617e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00380476, Final residual = 5.94688e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00380512, Final residual = 5.95278e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0044648, Final residual = 4.27825e-07, No Iterations 1 +min/max(T) = 676.245, 2438.96 +GAMG: Solving for p, Initial residual = 0.0703847, Final residual = 0.000759059, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.99002e-06, global = 5.25134e-06, cumulative = 0.00191414 +GAMG: Solving for p, Initial residual = 0.000717427, Final residual = 6.19333e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.53919e-06, global = 5.53713e-06, cumulative = 0.00191967 +smoothSolver: Solving for epsilon, Initial residual = 0.0015674, Final residual = 4.49457e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00257364, Final residual = 4.99e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.099663 s +other Time = 0 s +rho Equations = 0.00018 s +U Equations = 0.0013 s +Y Equations = 0.00246499 s +E Equations = 0.000606 s +p Equations = 0.002449 s +calculate parcels = 79.8825 s +chemistry correctThermo = 0.002862 s +turbulence correct = 0.001085 s +combustion correct(in Y) = 0.088511 s +percentage of chemistry = 88.8103 % +percentage of rho/U/Y/E = 4.56638 % +========Time details of each equation======= +rhoEqn Time = 0.000339 s +rhoEqn assamble = 0.000255 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001299 s +UEqn assamble = 0.000794 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000505 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001831 s +YEqn assamble = 0.000692 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000189 s +YEqn correct boundary = 0 s +EEqn Time = 0.000449 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 125.26 s ClockTime = 126 s +Courant Number mean: 0.00933986 max: 0.0383653 +Time = 0.0012275 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 22144 + Current mass in system = 1.6031e-09 + Linear momentum = (3.00093e-11 -1.19358e-08 0) + |Linear momentum| = 1.19359e-08 + Linear kinetic energy = 4.60663e-08 + model1: + number of parcels added = 22209 + mass introduced = 1.68698e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.135, 540.2 + Mass transfer phase change = 8.38781e-11 + D10, D32, Dmax (mu) = 56.421, 86.0899, 152.457 + Liquid penetration 95% mass (m) = 0.00883241 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00852822, Final residual = 1.24139e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0100755, Final residual = 7.54701e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00226586, Final residual = 3.39923e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00358466, Final residual = 5.3064e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00376601, Final residual = 5.87888e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00376637, Final residual = 5.88508e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0044447, Final residual = 4.25496e-07, No Iterations 1 +min/max(T) = 677.216, 2452.15 +GAMG: Solving for p, Initial residual = 0.0706487, Final residual = 0.000471288, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.80753e-06, global = 5.35939e-06, cumulative = 0.00192503 +GAMG: Solving for p, Initial residual = 0.000447268, Final residual = 2.12815e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.43596e-06, global = 5.4353e-06, cumulative = 0.00193047 +smoothSolver: Solving for epsilon, Initial residual = 0.00156875, Final residual = 4.54118e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00255508, Final residual = 4.9768e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.106628 s +other Time = 0 s +rho Equations = 0.000157 s +U Equations = 0.001083 s +Y Equations = 0.00244089 s +E Equations = 0.00061 s +p Equations = 0.002374 s +calculate parcels = 80.2444 s +chemistry correctThermo = 0.002825 s +turbulence correct = 0.001016 s +combustion correct(in Y) = 0.0959371 s +percentage of chemistry = 89.9737 % +percentage of rho/U/Y/E = 4.02417 % +========Time details of each equation======= +rhoEqn Time = 0.000293 s +rhoEqn assamble = 0.000232 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001083 s +UEqn assamble = 0.00067 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000413 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001882 s +YEqn assamble = 0.00066 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000246 s +YEqn correct boundary = 0 s +EEqn Time = 0.000451 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 125.73 s ClockTime = 126 s +Courant Number mean: 0.00942355 max: 0.0384519 +Time = 0.00123 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 49 new parcels + +Cloud: sprayCloud + Current number of parcels = 22190 + Current mass in system = 1.6047e-09 + Linear momentum = (2.97808e-11 -1.19433e-08 0) + |Linear momentum| = 1.19434e-08 + Linear kinetic energy = 4.60731e-08 + model1: + number of parcels added = 22258 + mass introduced = 1.68912e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.152, 540.2 + Mass transfer phase change = 8.44159e-11 + D10, D32, Dmax (mu) = 56.6536, 86.1387, 152.542 + Liquid penetration 95% mass (m) = 0.00884957 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00858204, Final residual = 1.37952e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00983914, Final residual = 7.30364e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00247935, Final residual = 3.89342e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00356582, Final residual = 5.26192e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00371271, Final residual = 5.81606e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00371308, Final residual = 5.82188e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00449914, Final residual = 4.39176e-07, No Iterations 1 +min/max(T) = 677.004, 2464.59 +GAMG: Solving for p, Initial residual = 0.0721323, Final residual = 0.000571271, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.16859e-06, global = 5.83131e-06, cumulative = 0.0019363 +GAMG: Solving for p, Initial residual = 0.000534329, Final residual = 5.27842e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.19992e-06, global = 6.19883e-06, cumulative = 0.0019425 +smoothSolver: Solving for epsilon, Initial residual = 0.00157735, Final residual = 4.5572e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00254401, Final residual = 4.93949e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.099078 s +other Time = 0 s +rho Equations = 0.000189 s +U Equations = 0.001035 s +Y Equations = 0.00267652 s +E Equations = 0.000674 s +p Equations = 0.002222 s +calculate parcels = 80.6167 s +chemistry correctThermo = 0.003099 s +turbulence correct = 0.000859 s +combustion correct(in Y) = 0.0881465 s +percentage of chemistry = 88.9668 % +percentage of rho/U/Y/E = 4.61709 % +========Time details of each equation======= +rhoEqn Time = 0.000324 s +rhoEqn assamble = 0.000257 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001035 s +UEqn assamble = 0.000568 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000467 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002099 s +YEqn assamble = 0.000758 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00026 s +YEqn correct boundary = 0 s +EEqn Time = 0.000507 s +EEqn assamble = 0.000374 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000133 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 126.2 s ClockTime = 127 s +Courant Number mean: 0.00948979 max: 0.0383927 +Time = 0.0012325 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 42 new parcels + +Cloud: sprayCloud + Current number of parcels = 22230 + Current mass in system = 1.60603e-09 + Linear momentum = (2.94425e-11 -1.19485e-08 0) + |Linear momentum| = 1.19486e-08 + Linear kinetic energy = 4.60708e-08 + model1: + number of parcels added = 22300 + mass introduced = 1.69092e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.133, 540.2 + Mass transfer phase change = 8.48923e-11 + D10, D32, Dmax (mu) = 56.9456, 86.1639, 152.625 + Liquid penetration 95% mass (m) = 0.00886657 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0091141, Final residual = 1.33734e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00957125, Final residual = 7.10165e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00220479, Final residual = 3.28445e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0035027, Final residual = 5.18089e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00367083, Final residual = 5.70897e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00367121, Final residual = 5.71452e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00442267, Final residual = 4.30769e-07, No Iterations 1 +min/max(T) = 676.865, 2476.39 +GAMG: Solving for p, Initial residual = 0.0730932, Final residual = 0.00050082, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.03464e-06, global = 5.49887e-06, cumulative = 0.001948 +GAMG: Solving for p, Initial residual = 0.000474064, Final residual = 3.57166e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.49116e-06, global = 5.49013e-06, cumulative = 0.00195349 +smoothSolver: Solving for epsilon, Initial residual = 0.00153787, Final residual = 4.45854e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00248979, Final residual = 9.83327e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.096101 s +other Time = 0 s +rho Equations = 0.000175 s +U Equations = 0.001188 s +Y Equations = 0.00248674 s +E Equations = 0.000609 s +p Equations = 0.002072 s +calculate parcels = 80.9745 s +chemistry correctThermo = 0.002234 s +turbulence correct = 0.000905 s +combustion correct(in Y) = 0.0862133 s +percentage of chemistry = 89.7111 % +percentage of rho/U/Y/E = 4.63964 % +========Time details of each equation======= +rhoEqn Time = 0.000297 s +rhoEqn assamble = 0.000235 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001188 s +UEqn assamble = 0.000693 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000495 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001851 s +YEqn assamble = 0.000666 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000204 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 126.66 s ClockTime = 127 s +Courant Number mean: 0.00955881 max: 0.038421 +Time = 0.001235 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 62 new parcels + +Cloud: sprayCloud + Current number of parcels = 22292 + Current mass in system = 1.60816e-09 + Linear momentum = (2.95362e-11 -1.19587e-08 0) + |Linear momentum| = 1.19587e-08 + Linear kinetic energy = 4.60841e-08 + model1: + number of parcels added = 22362 + mass introduced = 1.69353e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.14, 540.2 + Mass transfer phase change = 8.53657e-11 + D10, D32, Dmax (mu) = 56.9416, 86.1984, 152.71 + Liquid penetration 95% mass (m) = 0.00888449 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0073539, Final residual = 1.06355e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00920343, Final residual = 6.72286e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00215743, Final residual = 3.17539e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00346468, Final residual = 5.08768e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00362756, Final residual = 5.58587e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00362794, Final residual = 5.59155e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00436898, Final residual = 4.25576e-07, No Iterations 1 +min/max(T) = 676.794, 2487.8 +GAMG: Solving for p, Initial residual = 0.0735516, Final residual = 0.000331922, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.46317e-06, global = 5.44767e-06, cumulative = 0.00195894 +GAMG: Solving for p, Initial residual = 0.000314787, Final residual = 2.59931e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.45792e-06, global = 5.45727e-06, cumulative = 0.00196439 +smoothSolver: Solving for epsilon, Initial residual = 0.00152272, Final residual = 4.43071e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00245892, Final residual = 9.72634e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.104549 s +other Time = 0 s +rho Equations = 0.000176 s +U Equations = 0.001281 s +Y Equations = 0.00242445 s +E Equations = 0.000625 s +p Equations = 0.002473 s +calculate parcels = 81.3391 s +chemistry correctThermo = 0.002867 s +turbulence correct = 0.001012 s +combustion correct(in Y) = 0.0934875 s +percentage of chemistry = 89.4198 % +percentage of rho/U/Y/E = 4.31037 % +========Time details of each equation======= +rhoEqn Time = 0.000323 s +rhoEqn assamble = 0.000257 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00128 s +UEqn assamble = 0.000779 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000501 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001782 s +YEqn assamble = 0.000641 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000175 s +YEqn correct boundary = 0 s +EEqn Time = 0.000458 s +EEqn assamble = 0.000341 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 127.13 s ClockTime = 128 s +Courant Number mean: 0.00962961 max: 0.0382678 +Time = 0.0012375 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 58 new parcels + +Cloud: sprayCloud + Current number of parcels = 22346 + Current mass in system = 1.60999e-09 + Linear momentum = (2.90925e-11 -1.19667e-08 0) + |Linear momentum| = 1.19667e-08 + Linear kinetic energy = 4.60899e-08 + model1: + number of parcels added = 22420 + mass introduced = 1.69594e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.13, 540.2 + Mass transfer phase change = 8.59488e-11 + D10, D32, Dmax (mu) = 57.1269, 86.2586, 152.796 + Liquid penetration 95% mass (m) = 0.00890072 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0057416, Final residual = 9.07537e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00890543, Final residual = 6.49519e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00255636, Final residual = 4.31938e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00345699, Final residual = 5.10081e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00357289, Final residual = 5.48467e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00357328, Final residual = 5.49065e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00442599, Final residual = 4.41933e-07, No Iterations 1 +min/max(T) = 676.792, 2498.78 +GAMG: Solving for p, Initial residual = 0.0761028, Final residual = 0.000737447, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.87308e-06, global = 6.10313e-06, cumulative = 0.0019705 +GAMG: Solving for p, Initial residual = 0.000689658, Final residual = 6.95796e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.72076e-06, global = 6.71982e-06, cumulative = 0.00197722 +smoothSolver: Solving for epsilon, Initial residual = 0.00152525, Final residual = 4.42074e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00245746, Final residual = 9.68616e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.076336 s +other Time = 1e-06 s +rho Equations = 0.00017 s +U Equations = 0.00109 s +Y Equations = 0.00212287 s +E Equations = 0.000484 s +p Equations = 0.002121 s +calculate parcels = 81.639 s +chemistry correctThermo = 0.001926 s +turbulence correct = 0.000885 s +combustion correct(in Y) = 0.0673461 s +percentage of chemistry = 88.2233 % +percentage of rho/U/Y/E = 5.06559 % +========Time details of each equation======= +rhoEqn Time = 0.000303 s +rhoEqn assamble = 0.00024 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001088 s +UEqn assamble = 0.000682 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000406 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001557 s +YEqn assamble = 0.000537 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000131 s +YEqn correct boundary = 0 s +EEqn Time = 0.000368 s +EEqn assamble = 0.000276 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 127.5 s ClockTime = 128 s +Courant Number mean: 0.00968338 max: 0.0381278 +Time = 0.00124 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 52 new parcels + +Cloud: sprayCloud + Current number of parcels = 22397 + Current mass in system = 1.61161e-09 + Linear momentum = (2.91451e-11 -1.19729e-08 0) + |Linear momentum| = 1.1973e-08 + Linear kinetic energy = 4.60882e-08 + model1: + number of parcels added = 22472 + mass introduced = 1.69807e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.138, 540.2 + Mass transfer phase change = 8.64592e-11 + D10, D32, Dmax (mu) = 57.1405, 86.2983, 152.88 + Liquid penetration 95% mass (m) = 0.00891954 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00745848, Final residual = 1.11929e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00898524, Final residual = 6.75578e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00226274, Final residual = 3.55487e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00339409, Final residual = 4.95811e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00353787, Final residual = 5.43382e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00353826, Final residual = 5.43956e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00432738, Final residual = 4.2649e-07, No Iterations 1 +min/max(T) = 676.859, 2509.51 +GAMG: Solving for p, Initial residual = 0.0778419, Final residual = 0.000695732, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.97815e-06, global = 5.78495e-06, cumulative = 0.001983 +GAMG: Solving for p, Initial residual = 0.000652909, Final residual = 5.16528e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.8844e-06, global = 5.88288e-06, cumulative = 0.00198888 +smoothSolver: Solving for epsilon, Initial residual = 0.00147854, Final residual = 4.28304e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00240294, Final residual = 9.49239e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092629 s +other Time = 1e-06 s +rho Equations = 0.000177 s +U Equations = 0.001232 s +Y Equations = 0.00248176 s +E Equations = 0.000606 s +p Equations = 0.002374 s +calculate parcels = 81.9867 s +chemistry correctThermo = 0.002873 s +turbulence correct = 0.000969 s +combustion correct(in Y) = 0.0817102 s +percentage of chemistry = 88.2124 % +percentage of rho/U/Y/E = 4.85459 % +========Time details of each equation======= +rhoEqn Time = 0.000323 s +rhoEqn assamble = 0.000256 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001231 s +UEqn assamble = 0.000733 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000498 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001833 s +YEqn assamble = 0.000656 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000191 s +YEqn correct boundary = 0 s +EEqn Time = 0.000448 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 127.94 s ClockTime = 128 s +Courant Number mean: 0.00974647 max: 0.0378208 +Time = 0.0012425 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 42 new parcels + +Cloud: sprayCloud + Current number of parcels = 22439 + Current mass in system = 1.61283e-09 + Linear momentum = (2.93157e-11 -1.19763e-08 0) + |Linear momentum| = 1.19763e-08 + Linear kinetic energy = 4.60763e-08 + model1: + number of parcels added = 22514 + mass introduced = 1.69976e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.123, 540.2 + Mass transfer phase change = 8.69331e-11 + D10, D32, Dmax (mu) = 57.1276, 86.3225, 152.957 + Liquid penetration 95% mass (m) = 0.00893757 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00615571, Final residual = 9.10235e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00866884, Final residual = 6.63647e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0020824, Final residual = 3.1399e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00336725, Final residual = 4.9367e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00352201, Final residual = 5.42053e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0035224, Final residual = 5.42667e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00424982, Final residual = 4.13911e-07, No Iterations 1 +min/max(T) = 676.997, 2520.08 +GAMG: Solving for p, Initial residual = 0.07926, Final residual = 0.000618918, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.30281e-06, global = 5.35949e-06, cumulative = 0.00199424 +GAMG: Solving for p, Initial residual = 0.000585796, Final residual = 5.09123e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.46434e-06, global = 5.46291e-06, cumulative = 0.00199971 +smoothSolver: Solving for epsilon, Initial residual = 0.00147432, Final residual = 4.31791e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00239318, Final residual = 9.51736e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.10725 s +other Time = 1e-06 s +rho Equations = 0.000194 s +U Equations = 0.001188 s +Y Equations = 0.00248357 s +E Equations = 0.000609 s +p Equations = 0.00238 s +calculate parcels = 82.3338 s +chemistry correctThermo = 0.002856 s +turbulence correct = 0.000994 s +combustion correct(in Y) = 0.0963474 s +percentage of chemistry = 89.8344 % +percentage of rho/U/Y/E = 4.1721 % +========Time details of each equation======= +rhoEqn Time = 0.000337 s +rhoEqn assamble = 0.000252 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001187 s +UEqn assamble = 0.00068 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000507 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001833 s +YEqn assamble = 0.000665 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000181 s +YEqn correct boundary = 0 s +EEqn Time = 0.000454 s +EEqn assamble = 0.000339 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 128.4 s ClockTime = 129 s +Courant Number mean: 0.00982287 max: 0.0376897 +Time = 0.001245 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 40 new parcels + +Cloud: sprayCloud + Current number of parcels = 22476 + Current mass in system = 1.61382e-09 + Linear momentum = (2.94423e-11 -1.1978e-08 0) + |Linear momentum| = 1.1978e-08 + Linear kinetic energy = 4.60587e-08 + model1: + number of parcels added = 22554 + mass introduced = 1.70134e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.128, 540.2 + Mass transfer phase change = 8.75191e-11 + D10, D32, Dmax (mu) = 57.1812, 86.3671, 153.033 + Liquid penetration 95% mass (m) = 0.00895675 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00666366, Final residual = 1.23132e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00843314, Final residual = 6.46349e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00252534, Final residual = 4.0493e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00337994, Final residual = 4.99093e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00349294, Final residual = 5.44257e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00349342, Final residual = 5.44922e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00433288, Final residual = 4.26269e-07, No Iterations 1 +min/max(T) = 677.197, 2530.11 +GAMG: Solving for p, Initial residual = 0.0834718, Final residual = 0.000953553, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.34159e-06, global = 6.15474e-06, cumulative = 0.00200586 +GAMG: Solving for p, Initial residual = 0.000886383, Final residual = 2.123e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.75369e-06, global = 6.75327e-06, cumulative = 0.00201261 +smoothSolver: Solving for epsilon, Initial residual = 0.0015116, Final residual = 4.4053e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0024348, Final residual = 9.67153e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.089322 s +other Time = 0 s +rho Equations = 0.000163 s +U Equations = 0.001056 s +Y Equations = 0.002152 s +E Equations = 0.000493 s +p Equations = 0.002166 s +calculate parcels = 82.7218 s +chemistry correctThermo = 0.002028 s +turbulence correct = 0.000861 s +combustion correct(in Y) = 0.080218 s +percentage of chemistry = 89.8077 % +percentage of rho/U/Y/E = 4.32592 % +========Time details of each equation======= +rhoEqn Time = 0.000284 s +rhoEqn assamble = 0.000226 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001055 s +UEqn assamble = 0.000629 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000426 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00158 s +YEqn assamble = 0.00061 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000131 s +YEqn correct boundary = 0 s +EEqn Time = 0.000374 s +EEqn assamble = 0.000281 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 128.87 s ClockTime = 129 s +Courant Number mean: 0.00988369 max: 0.037832 +Time = 0.0012475 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 59 new parcels + +Cloud: sprayCloud + Current number of parcels = 22530 + Current mass in system = 1.61546e-09 + Linear momentum = (2.91583e-11 -1.19831e-08 0) + |Linear momentum| = 1.19832e-08 + Linear kinetic energy = 4.60496e-08 + model1: + number of parcels added = 22613 + mass introduced = 1.70361e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.136, 540.2 + Mass transfer phase change = 8.81502e-11 + D10, D32, Dmax (mu) = 57.4112, 86.4376, 153.11 + Liquid penetration 95% mass (m) = 0.00897608 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00896759, Final residual = 1.49968e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00841495, Final residual = 6.68544e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0026665, Final residual = 4.44847e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00335141, Final residual = 4.99003e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00344412, Final residual = 5.38571e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00344455, Final residual = 5.39199e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00436197, Final residual = 4.33924e-07, No Iterations 1 +min/max(T) = 677.475, 2539.74 +GAMG: Solving for p, Initial residual = 0.0868375, Final residual = 0.000885026, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.97147e-06, global = 6.7671e-06, cumulative = 0.00201938 +GAMG: Solving for p, Initial residual = 0.000843875, Final residual = 3.96908e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.27517e-06, global = 7.27459e-06, cumulative = 0.00202666 +smoothSolver: Solving for epsilon, Initial residual = 0.00149511, Final residual = 4.30397e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00242316, Final residual = 9.60024e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.106546 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.00121 s +Y Equations = 0.00257708 s +E Equations = 0.000611 s +p Equations = 0.002524 s +calculate parcels = 83.0974 s +chemistry correctThermo = 0.002812 s +turbulence correct = 0.001012 s +combustion correct(in Y) = 0.0954149 s +percentage of chemistry = 89.5528 % +percentage of rho/U/Y/E = 4.294 % +========Time details of each equation======= +rhoEqn Time = 0.000329 s +rhoEqn assamble = 0.000261 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001209 s +UEqn assamble = 0.000705 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000504 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001933 s +YEqn assamble = 0.000706 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000216 s +YEqn correct boundary = 0 s +EEqn Time = 0.000453 s +EEqn assamble = 0.00034 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 129.36 s ClockTime = 130 s +Courant Number mean: 0.00993045 max: 0.0377226 +Time = 0.00125 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 59 new parcels + +Cloud: sprayCloud + Current number of parcels = 22586 + Current mass in system = 1.61712e-09 + Linear momentum = (2.91697e-11 -1.19876e-08 0) + |Linear momentum| = 1.19877e-08 + Linear kinetic energy = 4.60355e-08 + model1: + number of parcels added = 22672 + mass introduced = 1.70585e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.116, 540.2 + Mass transfer phase change = 8.87317e-11 + D10, D32, Dmax (mu) = 57.5087, 86.4886, 153.184 + Liquid penetration 95% mass (m) = 0.00899264 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0108064, Final residual = 1.8177e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00849078, Final residual = 6.99435e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00244203, Final residual = 3.94444e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00329478, Final residual = 4.89139e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00340565, Final residual = 5.29002e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00340604, Final residual = 5.29565e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00428967, Final residual = 4.25265e-07, No Iterations 1 +min/max(T) = 677.806, 2549.3 +GAMG: Solving for p, Initial residual = 0.0900265, Final residual = 0.0010651, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.40356e-06, global = 6.61705e-06, cumulative = 0.00203327 +GAMG: Solving for p, Initial residual = 0.00101818, Final residual = 2.97865e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.70323e-06, global = 6.70258e-06, cumulative = 0.00203997 +smoothSolver: Solving for epsilon, Initial residual = 0.00144494, Final residual = 4.14268e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00237237, Final residual = 9.41976e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.0756 s +other Time = 0 s +rho Equations = 0.00017 s +U Equations = 0.001017 s +Y Equations = 0.00246674 s +E Equations = 0.000491 s +p Equations = 0.002154 s +calculate parcels = 83.4247 s +chemistry correctThermo = 0.001935 s +turbulence correct = 0.000963 s +combustion correct(in Y) = 0.0662213 s +percentage of chemistry = 87.5943 % +percentage of rho/U/Y/E = 5.48247 % +========Time details of each equation======= +rhoEqn Time = 0.000294 s +rhoEqn assamble = 0.000238 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001015 s +UEqn assamble = 0.000601 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000414 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001902 s +YEqn assamble = 0.000631 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000192 s +YEqn correct boundary = 0 s +EEqn Time = 0.000364 s +EEqn assamble = 0.000273 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 129.76 s ClockTime = 130 s +Courant Number mean: 0.00998978 max: 0.0370971 +Time = 0.0012525 + + +Solving 2-D cloud sprayCloud + +Cloud: sprayCloud injector: model1 + Added 39 new parcels + +Cloud: sprayCloud + Current number of parcels = 22624 + Current mass in system = 1.61692e-09 + Linear momentum = (2.93585e-11 -1.19809e-08 0) + |Linear momentum| = 1.19809e-08 + Linear kinetic energy = 4.59869e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.232, 540.2 + Mass transfer phase change = 8.92254e-11 + D10, D32, Dmax (mu) = 57.5465, 86.5181, 153.261 + Liquid penetration 95% mass (m) = 0.00901174 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0107801, Final residual = 1.7199e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00820996, Final residual = 6.83952e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00208779, Final residual = 3.24426e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00325897, Final residual = 4.82135e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0033978, Final residual = 5.26167e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0033982, Final residual = 5.26695e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00420978, Final residual = 4.06867e-07, No Iterations 1 +min/max(T) = 678.176, 2558.78 +GAMG: Solving for p, Initial residual = 0.0922803, Final residual = 0.00118658, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.57102e-06, global = 5.30132e-06, cumulative = 0.00204528 +GAMG: Solving for p, Initial residual = 0.00113185, Final residual = 8.90461e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.69251e-06, global = 5.69028e-06, cumulative = 0.00205097 +smoothSolver: Solving for epsilon, Initial residual = 0.00142715, Final residual = 4.11765e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00234458, Final residual = 9.33942e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.093783 s +other Time = 1e-06 s +rho Equations = 0.000153 s +U Equations = 0.000985 s +Y Equations = 0.0024531 s +E Equations = 0.000608 s +p Equations = 0.002456 s +calculate parcels = 83.7689 s +chemistry correctThermo = 0.002845 s +turbulence correct = 0.001041 s +combustion correct(in Y) = 0.0830689 s +percentage of chemistry = 88.5756 % +percentage of rho/U/Y/E = 4.47746 % +========Time details of each equation======= +rhoEqn Time = 0.000301 s +rhoEqn assamble = 0.000239 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000984 s +UEqn assamble = 0.000567 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000417 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001843 s +YEqn assamble = 0.000653 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00021 s +YEqn correct boundary = 0 s +EEqn Time = 0.000457 s +EEqn assamble = 0.000343 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 130.2 s ClockTime = 131 s +Courant Number mean: 0.0100635 max: 0.0369392 +Time = 0.001255 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22620 + Current mass in system = 1.61634e-09 + Linear momentum = (2.94843e-11 -1.19719e-08 0) + |Linear momentum| = 1.19719e-08 + Linear kinetic energy = 4.59314e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.35, 540.2 + Mass transfer phase change = 8.97981e-11 + D10, D32, Dmax (mu) = 57.7371, 86.5645, 153.34 + Liquid penetration 95% mass (m) = 0.00903078 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0103655, Final residual = 1.59549e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00797135, Final residual = 6.58066e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00238146, Final residual = 3.91926e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00328053, Final residual = 4.84052e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00338852, Final residual = 5.2293e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00338891, Final residual = 5.23496e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00427408, Final residual = 4.17114e-07, No Iterations 1 +min/max(T) = 678.594, 2567.74 +GAMG: Solving for p, Initial residual = 0.0972287, Final residual = 0.00106787, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.23635e-06, global = 6.26676e-06, cumulative = 0.00205723 +GAMG: Solving for p, Initial residual = 0.00100548, Final residual = 8.39493e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.60181e-06, global = 6.60055e-06, cumulative = 0.00206383 +smoothSolver: Solving for epsilon, Initial residual = 0.00147134, Final residual = 4.234e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00237813, Final residual = 9.44212e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.096901 s +other Time = 1e-06 s +rho Equations = 0.00015 s +U Equations = 0.001008 s +Y Equations = 0.00212625 s +E Equations = 0.000493 s +p Equations = 0.002491 s +calculate parcels = 84.1362 s +chemistry correctThermo = 0.002063 s +turbulence correct = 0.001 s +combustion correct(in Y) = 0.0873887 s +percentage of chemistry = 90.1835 % +percentage of rho/U/Y/E = 3.89805 % +========Time details of each equation======= +rhoEqn Time = 0.000298 s +rhoEqn assamble = 0.000236 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001006 s +UEqn assamble = 0.000555 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000451 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001558 s +YEqn assamble = 0.000544 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000154 s +YEqn correct boundary = 0 s +EEqn Time = 0.00037 s +EEqn assamble = 0.000278 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 130.66 s ClockTime = 131 s +Courant Number mean: 0.0101233 max: 0.0373256 +Time = 0.0012575 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22618 + Current mass in system = 1.6158e-09 + Linear momentum = (2.97382e-11 -1.19626e-08 0) + |Linear momentum| = 1.19627e-08 + Linear kinetic energy = 4.58741e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.469, 540.2 + Mass transfer phase change = 9.0341e-11 + D10, D32, Dmax (mu) = 57.7632, 86.6025, 153.421 + Liquid penetration 95% mass (m) = 0.00904929 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00896333, Final residual = 1.36733e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00748898, Final residual = 6.1831e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00225633, Final residual = 3.67434e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00325231, Final residual = 4.79442e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00337088, Final residual = 5.19354e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00337127, Final residual = 5.19931e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00424997, Final residual = 4.19323e-07, No Iterations 1 +min/max(T) = 679.066, 2576.03 +GAMG: Solving for p, Initial residual = 0.101128, Final residual = 0.000917727, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.26168e-06, global = 6.36898e-06, cumulative = 0.0020702 +GAMG: Solving for p, Initial residual = 0.000896015, Final residual = 6.54706e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.25923e-06, global = 6.25782e-06, cumulative = 0.00207646 +smoothSolver: Solving for epsilon, Initial residual = 0.00146169, Final residual = 4.20974e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00236349, Final residual = 9.39423e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.088048 s +other Time = 0 s +rho Equations = 0.000215 s +U Equations = 0.001323 s +Y Equations = 0.00254443 s +E Equations = 0.000633 s +p Equations = 0.002614 s +calculate parcels = 84.5114 s +chemistry correctThermo = 0.002812 s +turbulence correct = 0.001065 s +combustion correct(in Y) = 0.0766166 s +percentage of chemistry = 87.0168 % +percentage of rho/U/Y/E = 5.35553 % +========Time details of each equation======= +rhoEqn Time = 0.000361 s +rhoEqn assamble = 0.000284 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001321 s +UEqn assamble = 0.000764 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000557 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001833 s +YEqn assamble = 0.000684 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000169 s +YEqn correct boundary = 0 s +EEqn Time = 0.000472 s +EEqn assamble = 0.000355 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 131.13 s ClockTime = 132 s +Courant Number mean: 0.0101831 max: 0.0375536 +Time = 0.00126 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22617 + Current mass in system = 1.61532e-09 + Linear momentum = (2.97652e-11 -1.19537e-08 0) + |Linear momentum| = 1.19537e-08 + Linear kinetic energy = 4.58174e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.588, 540.2 + Mass transfer phase change = 9.08226e-11 + D10, D32, Dmax (mu) = 57.8601, 86.6283, 153.501 + Liquid penetration 95% mass (m) = 0.00906752 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00795332, Final residual = 1.2116e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0070736, Final residual = 5.71643e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00196813, Final residual = 3.06365e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00320949, Final residual = 4.72627e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00334458, Final residual = 5.14127e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00334497, Final residual = 5.14697e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00417673, Final residual = 4.04991e-07, No Iterations 1 +min/max(T) = 679.599, 2584.12 +GAMG: Solving for p, Initial residual = 0.104398, Final residual = 0.000949561, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.59979e-06, global = 5.26041e-06, cumulative = 0.00208172 +GAMG: Solving for p, Initial residual = 0.000912905, Final residual = 5.89104e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.5522e-06, global = 5.5509e-06, cumulative = 0.00208727 +smoothSolver: Solving for epsilon, Initial residual = 0.00143833, Final residual = 4.17735e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00233125, Final residual = 9.31634e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.093833 s +other Time = 0 s +rho Equations = 0.000149 s +U Equations = 0.001063 s +Y Equations = 0.00235662 s +E Equations = 0.00063 s +p Equations = 0.002446 s +calculate parcels = 84.8887 s +chemistry correctThermo = 0.002841 s +turbulence correct = 0.001146 s +combustion correct(in Y) = 0.0830184 s +percentage of chemistry = 88.4746 % +percentage of rho/U/Y/E = 4.47456 % +========Time details of each equation======= +rhoEqn Time = 0.000291 s +rhoEqn assamble = 0.00023 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001062 s +UEqn assamble = 0.000637 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000425 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001801 s +YEqn assamble = 0.000621 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000223 s +YEqn correct boundary = 0 s +EEqn Time = 0.000475 s +EEqn assamble = 0.000357 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 131.6 s ClockTime = 132 s +Courant Number mean: 0.0102513 max: 0.0376407 +Time = 0.0012625 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22614 + Current mass in system = 1.61473e-09 + Linear momentum = (2.97428e-11 -1.19442e-08 0) + |Linear momentum| = 1.19442e-08 + Linear kinetic energy = 4.57596e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.709, 540.2 + Mass transfer phase change = 9.1417e-11 + D10, D32, Dmax (mu) = 57.9249, 86.6802, 153.583 + Liquid penetration 95% mass (m) = 0.00908526 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00757821, Final residual = 1.13497e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00660698, Final residual = 5.09259e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00232883, Final residual = 3.89676e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0032079, Final residual = 4.77682e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00329995, Final residual = 5.11665e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00330035, Final residual = 5.12219e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00425375, Final residual = 4.28578e-07, No Iterations 1 +min/max(T) = 680.191, 2591.81 +GAMG: Solving for p, Initial residual = 0.110317, Final residual = 0.00106853, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.30194e-06, global = 6.38927e-06, cumulative = 0.00209366 +GAMG: Solving for p, Initial residual = 0.00102308, Final residual = 2.17489e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.85112e-06, global = 6.85075e-06, cumulative = 0.00210051 +smoothSolver: Solving for epsilon, Initial residual = 0.00143811, Final residual = 4.14751e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00231287, Final residual = 9.2138e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095184 s +other Time = 1e-06 s +rho Equations = 0.000181 s +U Equations = 0.001178 s +Y Equations = 0.00225016 s +E Equations = 0.000502 s +p Equations = 0.002277 s +calculate parcels = 85.2615 s +chemistry correctThermo = 0.002019 s +turbulence correct = 0.000914 s +combustion correct(in Y) = 0.0856628 s +percentage of chemistry = 89.9971 % +percentage of rho/U/Y/E = 4.31917 % +========Time details of each equation======= +rhoEqn Time = 0.000317 s +rhoEqn assamble = 0.000256 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001176 s +UEqn assamble = 0.000684 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000492 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001611 s +YEqn assamble = 0.000599 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000107 s +YEqn correct boundary = 0 s +EEqn Time = 0.000377 s +EEqn assamble = 0.000284 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 132.06 s ClockTime = 133 s +Courant Number mean: 0.0103003 max: 0.0376284 +Time = 0.001265 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22614 + Current mass in system = 1.61425e-09 + Linear momentum = (2.94503e-11 -1.19353e-08 0) + |Linear momentum| = 1.19353e-08 + Linear kinetic energy = 4.57036e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.829, 540.2 + Mass transfer phase change = 9.18948e-11 + D10, D32, Dmax (mu) = 57.8834, 86.7066, 153.664 + Liquid penetration 95% mass (m) = 0.00910246 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0082103, Final residual = 1.2e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00630876, Final residual = 4.69022e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00188163, Final residual = 2.88816e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00314888, Final residual = 4.64158e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00327855, Final residual = 5.03855e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00327895, Final residual = 5.04384e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00416229, Final residual = 4.0206e-07, No Iterations 1 +min/max(T) = 680.823, 2599.07 +GAMG: Solving for p, Initial residual = 0.11504, Final residual = 0.00112266, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.65001e-06, global = 5.36983e-06, cumulative = 0.00210588 +GAMG: Solving for p, Initial residual = 0.00108507, Final residual = 3.13576e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.50806e-06, global = 5.50756e-06, cumulative = 0.00211139 +smoothSolver: Solving for epsilon, Initial residual = 0.00141224, Final residual = 4.09949e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00227842, Final residual = 9.10748e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092194 s +other Time = 0 s +rho Equations = 0.000168 s +U Equations = 0.00107 s +Y Equations = 0.00204888 s +E Equations = 0.000485 s +p Equations = 0.002093 s +calculate parcels = 85.5261 s +chemistry correctThermo = 0.002043 s +turbulence correct = 0.000855 s +combustion correct(in Y) = 0.0832421 s +percentage of chemistry = 90.2902 % +percentage of rho/U/Y/E = 4.09125 % +========Time details of each equation======= +rhoEqn Time = 0.000289 s +rhoEqn assamble = 0.000229 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00107 s +UEqn assamble = 0.000658 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000412 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001497 s +YEqn assamble = 0.000525 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000133 s +YEqn correct boundary = 0 s +EEqn Time = 0.000365 s +EEqn assamble = 0.000271 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 132.42 s ClockTime = 133 s +Courant Number mean: 0.0103555 max: 0.0375749 +Time = 0.0012675 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22613 + Current mass in system = 1.61377e-09 + Linear momentum = (2.91956e-11 -1.19264e-08 0) + |Linear momentum| = 1.19265e-08 + Linear kinetic energy = 4.5648e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 380.951, 540.2 + Mass transfer phase change = 9.2374e-11 + D10, D32, Dmax (mu) = 58.0437, 86.7351, 153.746 + Liquid penetration 95% mass (m) = 0.00912118 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00601622, Final residual = 9.59116e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00577356, Final residual = 4.18091e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00186319, Final residual = 2.84954e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00312524, Final residual = 4.6609e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00325133, Final residual = 5.05939e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00325174, Final residual = 5.06477e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00411648, Final residual = 3.99337e-07, No Iterations 1 +min/max(T) = 681.51, 2605.98 +GAMG: Solving for p, Initial residual = 0.120341, Final residual = 0.000708196, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.87754e-06, global = 5.41935e-06, cumulative = 0.00211681 +GAMG: Solving for p, Initial residual = 0.000689081, Final residual = 5.10739e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.5232e-06, global = 5.52238e-06, cumulative = 0.00212233 +smoothSolver: Solving for epsilon, Initial residual = 0.00141452, Final residual = 4.13881e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0022742, Final residual = 9.13574e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.105444 s +other Time = 1e-06 s +rho Equations = 0.00018 s +U Equations = 0.00118 s +Y Equations = 0.00241408 s +E Equations = 0.000607 s +p Equations = 0.002418 s +calculate parcels = 85.8924 s +chemistry correctThermo = 0.002817 s +turbulence correct = 0.001093 s +combustion correct(in Y) = 0.0945369 s +percentage of chemistry = 89.656 % +percentage of rho/U/Y/E = 4.15488 % +========Time details of each equation======= +rhoEqn Time = 0.000329 s +rhoEqn assamble = 0.000251 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001178 s +UEqn assamble = 0.000678 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.0005 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001762 s +YEqn assamble = 0.000644 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000164 s +YEqn correct boundary = 0 s +EEqn Time = 0.000455 s +EEqn assamble = 0.00034 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 132.89 s ClockTime = 133 s +Courant Number mean: 0.0104101 max: 0.0376813 +Time = 0.00127 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22608 + Current mass in system = 1.61315e-09 + Linear momentum = (2.90019e-11 -1.19169e-08 0) + |Linear momentum| = 1.19169e-08 + Linear kinetic energy = 4.55906e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 381.072, 540.2 + Mass transfer phase change = 9.29935e-11 + D10, D32, Dmax (mu) = 58.1941, 86.7986, 153.831 + Liquid penetration 95% mass (m) = 0.00914062 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00538658, Final residual = 9.5561e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00527694, Final residual = 3.73627e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00239731, Final residual = 3.60376e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00312598, Final residual = 4.70852e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00320572, Final residual = 5.06794e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00320616, Final residual = 5.07346e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00420151, Final residual = 4.12723e-07, No Iterations 1 +min/max(T) = 682.274, 2612.28 +GAMG: Solving for p, Initial residual = 0.129209, Final residual = 0.00154338, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.74743e-06, global = 6.26517e-06, cumulative = 0.0021286 +GAMG: Solving for p, Initial residual = 0.00149174, Final residual = 2.88985e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.14044e-06, global = 7.14014e-06, cumulative = 0.00213574 +smoothSolver: Solving for epsilon, Initial residual = 0.00142418, Final residual = 4.12053e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00228323, Final residual = 9.13678e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.107901 s +other Time = 0 s +rho Equations = 0.000179 s +U Equations = 0.001142 s +Y Equations = 0.00248716 s +E Equations = 0.000601 s +p Equations = 0.002595 s +calculate parcels = 86.2524 s +chemistry correctThermo = 0.002848 s +turbulence correct = 0.001027 s +combustion correct(in Y) = 0.0968188 s +percentage of chemistry = 89.7293 % +percentage of rho/U/Y/E = 4.08631 % +========Time details of each equation======= +rhoEqn Time = 0.000325 s +rhoEqn assamble = 0.000257 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001142 s +UEqn assamble = 0.000655 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000487 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00185 s +YEqn assamble = 0.000659 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000202 s +YEqn correct boundary = 0 s +EEqn Time = 0.000444 s +EEqn assamble = 0.00033 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 133.36 s ClockTime = 134 s +Courant Number mean: 0.0104342 max: 0.0377573 +Time = 0.0012725 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22603 + Current mass in system = 1.61256e-09 + Linear momentum = (2.89119e-11 -1.19073e-08 0) + |Linear momentum| = 1.19073e-08 + Linear kinetic energy = 4.5532e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 381.193, 540.2 + Mass transfer phase change = 9.35803e-11 + D10, D32, Dmax (mu) = 58.4786, 86.8564, 153.915 + Liquid penetration 95% mass (m) = 0.0091597 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00893152, Final residual = 1.32677e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00532957, Final residual = 4.00455e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00223014, Final residual = 3.64916e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00307053, Final residual = 4.63792e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0031678, Final residual = 5.02537e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00316821, Final residual = 5.03042e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00415031, Final residual = 4.0643e-07, No Iterations 1 +min/max(T) = 683.101, 2618.54 +GAMG: Solving for p, Initial residual = 0.137988, Final residual = 0.00139246, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.03686e-06, global = 6.52411e-06, cumulative = 0.00214226 +GAMG: Solving for p, Initial residual = 0.00136212, Final residual = 8.22083e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.76512e-06, global = 6.76366e-06, cumulative = 0.00214902 +smoothSolver: Solving for epsilon, Initial residual = 0.00137609, Final residual = 3.96736e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00223675, Final residual = 8.95839e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.123456 s +other Time = 0 s +rho Equations = 0.000159 s +U Equations = 0.001059 s +Y Equations = 0.00209974 s +E Equations = 0.000495 s +p Equations = 0.001977 s +calculate parcels = 86.6189 s +chemistry correctThermo = 0.002079 s +turbulence correct = 0.00083 s +combustion correct(in Y) = 0.114572 s +percentage of chemistry = 92.8041 % +percentage of rho/U/Y/E = 3.08834 % +========Time details of each equation======= +rhoEqn Time = 0.000281 s +rhoEqn assamble = 0.000223 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001058 s +UEqn assamble = 0.000625 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000433 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001523 s +YEqn assamble = 0.00054 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000134 s +YEqn correct boundary = 0 s +EEqn Time = 0.000372 s +EEqn assamble = 0.000276 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 133.85 s ClockTime = 134 s +Courant Number mean: 0.0104564 max: 0.0375115 +Time = 0.001275 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22599 + Current mass in system = 1.61203e-09 + Linear momentum = (2.88563e-11 -1.18976e-08 0) + |Linear momentum| = 1.18977e-08 + Linear kinetic energy = 4.54718e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 381.314, 540.2 + Mass transfer phase change = 9.41164e-11 + D10, D32, Dmax (mu) = 58.7671, 86.9021, 154.002 + Liquid penetration 95% mass (m) = 0.00917717 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00990874, Final residual = 1.38495e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0050525, Final residual = 4.08344e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00197712, Final residual = 2.90764e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00301547, Final residual = 4.55558e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00311688, Final residual = 4.91692e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00311729, Final residual = 4.92171e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00406723, Final residual = 3.90804e-07, No Iterations 1 +min/max(T) = 683.959, 2624.98 +GAMG: Solving for p, Initial residual = 0.146251, Final residual = 0.00176363, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.78527e-06, global = 5.90379e-06, cumulative = 0.00215493 +GAMG: Solving for p, Initial residual = 0.0017606, Final residual = 3.09369e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.17936e-06, global = 6.17887e-06, cumulative = 0.00216111 +smoothSolver: Solving for epsilon, Initial residual = 0.00133034, Final residual = 3.83384e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00218856, Final residual = 8.76672e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.099051 s +other Time = 0 s +rho Equations = 0.000173 s +U Equations = 0.00127 s +Y Equations = 0.00210313 s +E Equations = 0.000491 s +p Equations = 0.002061 s +calculate parcels = 86.9941 s +chemistry correctThermo = 0.002032 s +turbulence correct = 0.000818 s +combustion correct(in Y) = 0.0899099 s +percentage of chemistry = 90.7713 % +percentage of rho/U/Y/E = 4.07581 % +========Time details of each equation======= +rhoEqn Time = 0.000288 s +rhoEqn assamble = 0.000226 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001269 s +UEqn assamble = 0.000753 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000516 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.0014 s +YEqn assamble = 0.000526 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 6e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.00037 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 134.33 s ClockTime = 135 s +Courant Number mean: 0.0104848 max: 0.0370027 +Time = 0.0012775 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22597 + Current mass in system = 1.6115e-09 + Linear momentum = (2.88177e-11 -1.18879e-08 0) + |Linear momentum| = 1.18879e-08 + Linear kinetic energy = 4.54105e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 381.437, 540.2 + Mass transfer phase change = 9.4643e-11 + D10, D32, Dmax (mu) = 58.8229, 86.9444, 154.089 + Liquid penetration 95% mass (m) = 0.0091959 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0111196, Final residual = 1.50838e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00485415, Final residual = 4.15026e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0019401, Final residual = 2.97124e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00299131, Final residual = 4.498e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00309157, Final residual = 4.86031e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00309197, Final residual = 4.86504e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00404738, Final residual = 3.91236e-07, No Iterations 1 +min/max(T) = 684.846, 2631.35 +GAMG: Solving for p, Initial residual = 0.156046, Final residual = 0.00146701, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.95958e-06, global = 5.87485e-06, cumulative = 0.00216698 +GAMG: Solving for p, Initial residual = 0.00145541, Final residual = 7.71081e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.0706e-06, global = 6.06959e-06, cumulative = 0.00217305 +smoothSolver: Solving for epsilon, Initial residual = 0.00133899, Final residual = 3.83904e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00218445, Final residual = 8.72125e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.076619 s +other Time = 0 s +rho Equations = 0.00016 s +U Equations = 0.001158 s +Y Equations = 0.00270444 s +E Equations = 0.000539 s +p Equations = 0.00252 s +calculate parcels = 87.2936 s +chemistry correctThermo = 0.002104 s +turbulence correct = 0.000938 s +combustion correct(in Y) = 0.0662946 s +percentage of chemistry = 86.525 % +percentage of rho/U/Y/E = 5.9534 % +========Time details of each equation======= +rhoEqn Time = 0.000296 s +rhoEqn assamble = 0.000232 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001157 s +UEqn assamble = 0.000674 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000483 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002118 s +YEqn assamble = 0.000645 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000207 s +YEqn correct boundary = 0 s +EEqn Time = 0.000396 s +EEqn assamble = 0.000302 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 134.7 s ClockTime = 135 s +Courant Number mean: 0.0105101 max: 0.0366419 +Time = 0.00128 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22594 + Current mass in system = 1.61093e-09 + Linear momentum = (2.86588e-11 -1.18774e-08 0) + |Linear momentum| = 1.18775e-08 + Linear kinetic energy = 4.53461e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 381.561, 540.2 + Mass transfer phase change = 9.52171e-11 + D10, D32, Dmax (mu) = 58.936, 86.991, 154.179 + Liquid penetration 95% mass (m) = 0.00921456 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0101398, Final residual = 1.46917e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00452005, Final residual = 4.00129e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0020553, Final residual = 3.40808e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00297565, Final residual = 4.45591e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00305978, Final residual = 4.76206e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0030602, Final residual = 4.76639e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00406478, Final residual = 3.96806e-07, No Iterations 1 +min/max(T) = 685.785, 2637.15 +GAMG: Solving for p, Initial residual = 0.168794, Final residual = 0.00169766, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.10845e-06, global = 6.1716e-06, cumulative = 0.00217922 +GAMG: Solving for p, Initial residual = 0.00169931, Final residual = 9.84764e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.61777e-06, global = 6.61718e-06, cumulative = 0.00218584 +smoothSolver: Solving for epsilon, Initial residual = 0.00131657, Final residual = 3.72061e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0021516, Final residual = 8.53676e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094887 s +other Time = 1e-06 s +rho Equations = 0.00025 s +U Equations = 0.001712 s +Y Equations = 0.00229496 s +E Equations = 0.000516 s +p Equations = 0.002579 s +calculate parcels = 87.6142 s +chemistry correctThermo = 0.002112 s +turbulence correct = 0.001053 s +combustion correct(in Y) = 0.084008 s +percentage of chemistry = 88.5348 % +percentage of rho/U/Y/E = 5.03015 % +========Time details of each equation======= +rhoEqn Time = 0.000407 s +rhoEqn assamble = 0.000312 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001711 s +UEqn assamble = 0.000906 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000805 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001227 s +YEqn assamble = 0.000508 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -0.000115 s +YEqn correct boundary = 0 s +EEqn Time = 0.000399 s +EEqn assamble = 0.0003 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 135.12 s ClockTime = 136 s +Courant Number mean: 0.0105273 max: 0.0367417 +Time = 0.0012825 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22591 + Current mass in system = 1.61036e-09 + Linear momentum = (2.86245e-11 -1.18669e-08 0) + |Linear momentum| = 1.18669e-08 + Linear kinetic energy = 4.5281e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 381.686, 540.2 + Mass transfer phase change = 9.57823e-11 + D10, D32, Dmax (mu) = 59.043, 87.0431, 154.268 + Liquid penetration 95% mass (m) = 0.0092336 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0103232, Final residual = 1.60239e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00437264, Final residual = 4.12616e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00198128, Final residual = 3.13244e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00293132, Final residual = 4.4092e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00301564, Final residual = 4.68261e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00301603, Final residual = 4.68677e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0040291, Final residual = 4.0124e-07, No Iterations 1 +min/max(T) = 686.78, 2643.07 +GAMG: Solving for p, Initial residual = 0.184668, Final residual = 0.00194343, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.68181e-06, global = 6.18251e-06, cumulative = 0.00219202 +GAMG: Solving for p, Initial residual = 0.00201583, Final residual = 3.85537e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.51462e-06, global = 6.51414e-06, cumulative = 0.00219854 +smoothSolver: Solving for epsilon, Initial residual = 0.00130812, Final residual = 3.68976e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0021305, Final residual = 8.43309e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103181 s +other Time = 0 s +rho Equations = 0.000159 s +U Equations = 0.001059 s +Y Equations = 0.00232354 s +E Equations = 0.000593 s +p Equations = 0.002582 s +calculate parcels = 87.9695 s +chemistry correctThermo = 0.002839 s +turbulence correct = 0.000956 s +combustion correct(in Y) = 0.0924805 s +percentage of chemistry = 89.6294 % +percentage of rho/U/Y/E = 4.00707 % +========Time details of each equation======= +rhoEqn Time = 0.000302 s +rhoEqn assamble = 0.000239 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001059 s +UEqn assamble = 0.000656 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000403 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001772 s +YEqn assamble = 0.000625 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000219 s +YEqn correct boundary = 0 s +EEqn Time = 0.00044 s +EEqn assamble = 0.00033 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00011 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 135.58 s ClockTime = 136 s +Courant Number mean: 0.0105365 max: 0.0367177 +Time = 0.001285 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22589 + Current mass in system = 1.60982e-09 + Linear momentum = (2.84824e-11 -1.18564e-08 0) + |Linear momentum| = 1.18564e-08 + Linear kinetic energy = 4.52149e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 381.811, 540.2 + Mass transfer phase change = 9.63198e-11 + D10, D32, Dmax (mu) = 59.1428, 87.0827, 154.353 + Liquid penetration 95% mass (m) = 0.0092541 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00968195, Final residual = 1.48206e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00415734, Final residual = 3.91408e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00190442, Final residual = 2.96757e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00288359, Final residual = 4.25653e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00297531, Final residual = 4.57894e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00297569, Final residual = 4.58303e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00395738, Final residual = 3.82907e-07, No Iterations 1 +min/max(T) = 687.808, 2648.62 +GAMG: Solving for p, Initial residual = 0.200644, Final residual = 0.00180649, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.18441e-06, global = 6.10258e-06, cumulative = 0.00220464 +GAMG: Solving for p, Initial residual = 0.0019194, Final residual = 4.50803e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.19602e-06, global = 6.19567e-06, cumulative = 0.00221083 +smoothSolver: Solving for epsilon, Initial residual = 0.00128492, Final residual = 3.64039e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00210103, Final residual = 8.32657e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100273 s +other Time = 0 s +rho Equations = 0.000159 s +U Equations = 0.000996 s +Y Equations = 0.00253201 s +E Equations = 0.000585 s +p Equations = 0.002549 s +calculate parcels = 88.3283 s +chemistry correctThermo = 0.002863 s +turbulence correct = 0.000973 s +combustion correct(in Y) = 0.089439 s +percentage of chemistry = 89.1955 % +percentage of rho/U/Y/E = 4.26038 % +========Time details of each equation======= +rhoEqn Time = 0.000299 s +rhoEqn assamble = 0.000237 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000994 s +UEqn assamble = 0.000567 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000427 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001862 s +YEqn assamble = 0.000658 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000193 s +YEqn correct boundary = 0 s +EEqn Time = 0.00043 s +EEqn assamble = 0.00032 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00011 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 136.04 s ClockTime = 137 s +Courant Number mean: 0.0105539 max: 0.0366586 +Time = 0.0012875 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22589 + Current mass in system = 1.60933e-09 + Linear momentum = (2.83869e-11 -1.1846e-08 0) + |Linear momentum| = 1.1846e-08 + Linear kinetic energy = 4.51486e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 381.937, 540.2 + Mass transfer phase change = 9.68097e-11 + D10, D32, Dmax (mu) = 59.0918, 87.1113, 154.439 + Liquid penetration 95% mass (m) = 0.00927336 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00728802, Final residual = 1.1745e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00385635, Final residual = 3.60698e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00170131, Final residual = 2.43762e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00283652, Final residual = 4.2217e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00293916, Final residual = 4.55225e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00293955, Final residual = 4.55637e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00388171, Final residual = 3.68893e-07, No Iterations 1 +min/max(T) = 688.885, 2653.9 +GAMG: Solving for p, Initial residual = 0.220746, Final residual = 0.00184791, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.57623e-06, global = 5.52965e-06, cumulative = 0.00221636 +GAMG: Solving for p, Initial residual = 0.00195665, Final residual = 2.12615e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.64683e-06, global = 5.64663e-06, cumulative = 0.00222201 +smoothSolver: Solving for epsilon, Initial residual = 0.00127505, Final residual = 3.63391e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00208066, Final residual = 8.26659e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100151 s +other Time = 0 s +rho Equations = 0.00017 s +U Equations = 0.001024 s +Y Equations = 0.002392 s +E Equations = 0.000643 s +p Equations = 0.002749 s +calculate parcels = 88.6822 s +chemistry correctThermo = 0.002843 s +turbulence correct = 0.00096 s +combustion correct(in Y) = 0.089178 s +percentage of chemistry = 89.0435 % +percentage of rho/U/Y/E = 4.22262 % +========Time details of each equation======= +rhoEqn Time = 0.000344 s +rhoEqn assamble = 0.000267 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001022 s +UEqn assamble = 0.000607 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000415 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001843 s +YEqn assamble = 0.000634 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000244 s +YEqn correct boundary = 0 s +EEqn Time = 0.000483 s +EEqn assamble = 0.000362 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000121 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 136.49 s ClockTime = 137 s +Courant Number mean: 0.0105801 max: 0.0367618 +Time = 0.00129 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22588 + Current mass in system = 1.6088e-09 + Linear momentum = (2.81643e-11 -1.18353e-08 0) + |Linear momentum| = 1.18353e-08 + Linear kinetic energy = 4.50813e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 382.063, 540.2 + Mass transfer phase change = 9.73448e-11 + D10, D32, Dmax (mu) = 59.0555, 87.1472, 154.527 + Liquid penetration 95% mass (m) = 0.0092936 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00608296, Final residual = 9.71577e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00344896, Final residual = 9.12473e-07, No Iterations 1 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00186314, Final residual = 2.86301e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00281664, Final residual = 4.18957e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00290176, Final residual = 4.50578e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00290216, Final residual = 4.51024e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00390046, Final residual = 3.7471e-07, No Iterations 1 +min/max(T) = 690.023, 2658.58 +GAMG: Solving for p, Initial residual = 0.248622, Final residual = 0.00179265, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.29508e-06, global = 6.02342e-06, cumulative = 0.00222803 +GAMG: Solving for p, Initial residual = 0.00189314, Final residual = 3.78415e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.16741e-06, global = 6.16726e-06, cumulative = 0.0022342 +smoothSolver: Solving for epsilon, Initial residual = 0.00127785, Final residual = 3.62558e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00207686, Final residual = 8.24072e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.075366 s +other Time = 0 s +rho Equations = 0.00017 s +U Equations = 0.001017 s +Y Equations = 0.00234885 s +E Equations = 0.000496 s +p Equations = 0.00225 s +calculate parcels = 89.0362 s +chemistry correctThermo = 0.002005 s +turbulence correct = 0.000841 s +combustion correct(in Y) = 0.0660352 s +percentage of chemistry = 87.6193 % +percentage of rho/U/Y/E = 5.34969 % +========Time details of each equation======= +rhoEqn Time = 0.000296 s +rhoEqn assamble = 0.000235 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001017 s +UEqn assamble = 0.000636 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000381 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001763 s +YEqn assamble = 0.000566 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000204 s +YEqn correct boundary = 0 s +EEqn Time = 0.000372 s +EEqn assamble = 0.000276 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 136.92 s ClockTime = 137 s +Courant Number mean: 0.0105969 max: 0.0371425 +Time = 0.0012925 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22585 + Current mass in system = 1.60821e-09 + Linear momentum = (2.80025e-11 -1.18241e-08 0) + |Linear momentum| = 1.18241e-08 + Linear kinetic energy = 4.5012e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 382.191, 540.2 + Mass transfer phase change = 9.79323e-11 + D10, D32, Dmax (mu) = 59.1526, 87.1964, 154.614 + Liquid penetration 95% mass (m) = 0.00931184 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00506184, Final residual = 8.00198e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00317604, Final residual = 8.447e-07, No Iterations 1 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00202349, Final residual = 3.07492e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00278656, Final residual = 4.13709e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00285493, Final residual = 4.44068e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00285534, Final residual = 4.44538e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00391987, Final residual = 3.76621e-07, No Iterations 1 +min/max(T) = 691.215, 2662.88 +GAMG: Solving for p, Initial residual = 0.282207, Final residual = 0.00205162, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.8502e-06, global = 6.48972e-06, cumulative = 0.00224069 +GAMG: Solving for p, Initial residual = 0.00225644, Final residual = 4.44991e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.77166e-06, global = 6.77141e-06, cumulative = 0.00224746 +smoothSolver: Solving for epsilon, Initial residual = 0.0012533, Final residual = 3.53078e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00204944, Final residual = 8.11294e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.113997 s +other Time = 1e-06 s +rho Equations = 0.000189 s +U Equations = 0.001136 s +Y Equations = 0.00229841 s +E Equations = 0.000586 s +p Equations = 0.002611 s +calculate parcels = 89.3078 s +chemistry correctThermo = 0.002828 s +turbulence correct = 0.001013 s +combustion correct(in Y) = 0.103122 s +percentage of chemistry = 90.4599 % +percentage of rho/U/Y/E = 3.69257 % +========Time details of each equation======= +rhoEqn Time = 0.000329 s +rhoEqn assamble = 0.000257 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001134 s +UEqn assamble = 0.000689 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000445 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001651 s +YEqn assamble = 0.000622 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000153 s +YEqn correct boundary = 0 s +EEqn Time = 0.000432 s +EEqn assamble = 0.000322 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00011 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 137.3 s ClockTime = 138 s +Courant Number mean: 0.0105985 max: 0.0372949 +Time = 0.001295 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22580 + Current mass in system = 1.60755e-09 + Linear momentum = (2.7727e-11 -1.18123e-08 0) + |Linear momentum| = 1.18124e-08 + Linear kinetic energy = 4.494e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 382.319, 540.2 + Mass transfer phase change = 9.85933e-11 + D10, D32, Dmax (mu) = 59.2392, 87.2614, 154.696 + Liquid penetration 95% mass (m) = 0.0093298 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00733043, Final residual = 1.12781e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0031783, Final residual = 8.60475e-07, No Iterations 1 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00226168, Final residual = 3.76624e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00274738, Final residual = 4.04972e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0027943, Final residual = 4.32866e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00279469, Final residual = 4.33306e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00393223, Final residual = 3.79321e-07, No Iterations 1 +min/max(T) = 692.448, 2671.95 +GAMG: Solving for p, Initial residual = 0.328784, Final residual = 0.00376177, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.48021e-06, global = 7.07103e-06, cumulative = 0.00225453 +GAMG: Solving for p, Initial residual = 0.0042535, Final residual = 2.62724e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.61855e-06, global = 7.61843e-06, cumulative = 0.00226215 +smoothSolver: Solving for epsilon, Initial residual = 0.00121855, Final residual = 3.37445e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00200756, Final residual = 7.87468e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.109339 s +other Time = 0 s +rho Equations = 0.000225 s +U Equations = 0.001635 s +Y Equations = 0.0025801 s +E Equations = 0.000604 s +p Equations = 0.002577 s +calculate parcels = 89.6638 s +chemistry correctThermo = 0.002866 s +turbulence correct = 0.001014 s +combustion correct(in Y) = 0.0976009 s +percentage of chemistry = 89.2645 % +percentage of rho/U/Y/E = 4.61327 % +========Time details of each equation======= +rhoEqn Time = 0.00036 s +rhoEqn assamble = 0.000274 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001633 s +UEqn assamble = 0.000888 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000745 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001573 s +YEqn assamble = 0.000628 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 1e-06 s +YEqn correct boundary = 0 s +EEqn Time = 0.000449 s +EEqn assamble = 0.000327 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000122 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 137.77 s ClockTime = 138 s +Courant Number mean: 0.0105854 max: 0.0370406 +Time = 0.0012975 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22579 + Current mass in system = 1.60703e-09 + Linear momentum = (2.74065e-11 -1.18011e-08 0) + |Linear momentum| = 1.18012e-08 + Linear kinetic energy = 4.48685e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 382.447, 540.2 + Mass transfer phase change = 9.91154e-11 + D10, D32, Dmax (mu) = 59.2514, 87.2993, 154.778 + Liquid penetration 95% mass (m) = 0.00935025 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00954828, Final residual = 1.39088e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00326466, Final residual = 9.01163e-07, No Iterations 1 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0017087, Final residual = 2.30249e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00267697, Final residual = 3.93104e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00276195, Final residual = 4.21095e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00276233, Final residual = 4.21508e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00382566, Final residual = 3.60451e-07, No Iterations 1 +min/max(T) = 693.683, 2681.51 +GAMG: Solving for p, Initial residual = 0.375325, Final residual = 0.00579062, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.72684e-06, global = 5.69042e-06, cumulative = 0.00226784 +GAMG: Solving for p, Initial residual = 0.00649424, Final residual = 2.24122e-07, No Iterations 6 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.01797e-06, global = 6.01785e-06, cumulative = 0.00227386 +smoothSolver: Solving for epsilon, Initial residual = 0.00118035, Final residual = 3.28528e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00194803, Final residual = 7.63414e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.098157 s +other Time = 1e-06 s +rho Equations = 0.000151 s +U Equations = 0.000927 s +Y Equations = 0.00237978 s +E Equations = 0.00059 s +p Equations = 0.002364 s +calculate parcels = 90.0172 s +chemistry correctThermo = 0.002861 s +turbulence correct = 0.000816 s +combustion correct(in Y) = 0.0878462 s +percentage of chemistry = 89.4956 % +percentage of rho/U/Y/E = 4.12378 % +========Time details of each equation======= +rhoEqn Time = 0.000268 s +rhoEqn assamble = 0.000213 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000927 s +UEqn assamble = 0.000567 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00036 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001825 s +YEqn assamble = 0.000616 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000239 s +YEqn correct boundary = 0 s +EEqn Time = 0.000434 s +EEqn assamble = 0.000325 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000109 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 138.22 s ClockTime = 139 s +Courant Number mean: 0.0105893 max: 0.0366317 +Time = 0.0013 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22577 + Current mass in system = 1.6064e-09 + Linear momentum = (2.71776e-11 -1.17892e-08 0) + |Linear momentum| = 1.17892e-08 + Linear kinetic energy = 4.47941e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 382.577, 540.2 + Mass transfer phase change = 9.97392e-11 + D10, D32, Dmax (mu) = 59.2395, 87.348, 154.864 + Liquid penetration 95% mass (m) = 0.00936943 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00908458, Final residual = 1.37122e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00303733, Final residual = 8.81069e-07, No Iterations 1 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00207783, Final residual = 3.21551e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00265694, Final residual = 3.869e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00271096, Final residual = 4.14355e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00271136, Final residual = 4.14792e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00387129, Final residual = 3.71698e-07, No Iterations 1 +min/max(T) = 694.948, 2690.67 +GAMG: Solving for p, Initial residual = 0.412796, Final residual = 0.00476494, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.27941e-06, global = 6.89427e-06, cumulative = 0.00228076 +GAMG: Solving for p, Initial residual = 0.00527968, Final residual = 2.23037e-07, No Iterations 6 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.19078e-06, global = 7.19068e-06, cumulative = 0.00228795 +smoothSolver: Solving for epsilon, Initial residual = 0.00120384, Final residual = 3.32795e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00194184, Final residual = 7.56259e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.106732 s +other Time = 1e-06 s +rho Equations = 0.000178 s +U Equations = 0.001134 s +Y Equations = 0.00238851 s +E Equations = 0.000606 s +p Equations = 0.002822 s +calculate parcels = 90.3774 s +chemistry correctThermo = 0.002849 s +turbulence correct = 0.001014 s +combustion correct(in Y) = 0.0955115 s +percentage of chemistry = 89.4872 % +percentage of rho/U/Y/E = 4.03488 % +========Time details of each equation======= +rhoEqn Time = 0.000319 s +rhoEqn assamble = 0.000248 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001134 s +UEqn assamble = 0.000715 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000419 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001777 s +YEqn assamble = 0.000615 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000197 s +YEqn correct boundary = 0 s +EEqn Time = 0.000452 s +EEqn assamble = 0.000324 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000128 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 139.03 s ClockTime = 140 s +Courant Number mean: 0.0105817 max: 0.0359609 +Time = 0.0013025 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22576 + Current mass in system = 1.60584e-09 + Linear momentum = (2.65726e-11 -1.17771e-08 0) + |Linear momentum| = 1.17771e-08 + Linear kinetic energy = 4.47178e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 382.708, 540.2 + Mass transfer phase change = 1.00301e-10 + D10, D32, Dmax (mu) = 59.2029, 87.389, 154.951 + Liquid penetration 95% mass (m) = 0.00938772 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0110925, Final residual = 1.61715e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00304985, Final residual = 9.28538e-07, No Iterations 1 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00181692, Final residual = 2.6122e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00260339, Final residual = 3.78127e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00267059, Final residual = 4.04187e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00267098, Final residual = 4.04617e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00384706, Final residual = 3.62655e-07, No Iterations 1 +min/max(T) = 696.263, 2698.93 +GAMG: Solving for p, Initial residual = 0.439546, Final residual = 0.00551807, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.60052e-06, global = 6.15454e-06, cumulative = 0.0022941 +GAMG: Solving for p, Initial residual = 0.00639026, Final residual = 2.60129e-07, No Iterations 6 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.4793e-06, global = 6.47924e-06, cumulative = 0.00230058 +smoothSolver: Solving for epsilon, Initial residual = 0.00118255, Final residual = 3.23407e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00191654, Final residual = 7.39775e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.083564 s +other Time = 0 s +rho Equations = 0.000224 s +U Equations = 0.001335 s +Y Equations = 0.00217712 s +E Equations = 0.000478 s +p Equations = 0.002321 s +calculate parcels = 90.6982 s +chemistry correctThermo = 0.00195 s +turbulence correct = 0.000813 s +combustion correct(in Y) = 0.0740179 s +percentage of chemistry = 88.5763 % +percentage of rho/U/Y/E = 5.04299 % +========Time details of each equation======= +rhoEqn Time = 0.000356 s +rhoEqn assamble = 0.000282 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001334 s +UEqn assamble = 0.000888 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000446 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001455 s +YEqn assamble = 0.000521 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 4.6e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000355 s +EEqn assamble = 0.000264 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 139.43 s ClockTime = 140 s +Courant Number mean: 0.0105633 max: 0.0358706 +Time = 0.001305 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22576 + Current mass in system = 1.60531e-09 + Linear momentum = (2.60245e-11 -1.1765e-08 0) + |Linear momentum| = 1.1765e-08 + Linear kinetic energy = 4.46408e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 382.84, 540.2 + Mass transfer phase change = 1.00832e-10 + D10, D32, Dmax (mu) = 59.1439, 87.4245, 155.037 + Liquid penetration 95% mass (m) = 0.00940641 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0104081, Final residual = 1.49801e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00294198, Final residual = 9.25753e-07, No Iterations 1 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00167528, Final residual = 2.13717e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00256966, Final residual = 3.71596e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00264399, Final residual = 3.98196e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00264438, Final residual = 3.9861e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00377139, Final residual = 3.52952e-07, No Iterations 1 +min/max(T) = 697.668, 2706.98 +GAMG: Solving for p, Initial residual = 0.419754, Final residual = 0.00318493, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.78505e-06, global = 6.03936e-06, cumulative = 0.00230662 +GAMG: Solving for p, Initial residual = 0.00389398, Final residual = 2.82236e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.1167e-06, global = 6.11659e-06, cumulative = 0.00231274 +smoothSolver: Solving for epsilon, Initial residual = 0.00115485, Final residual = 3.13716e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00188056, Final residual = 7.22699e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.091077 s +other Time = 0 s +rho Equations = 0.000179 s +U Equations = 0.001092 s +Y Equations = 0.00214612 s +E Equations = 0.000492 s +p Equations = 0.002264 s +calculate parcels = 90.9915 s +chemistry correctThermo = 0.002083 s +turbulence correct = 0.000843 s +combustion correct(in Y) = 0.0817729 s +percentage of chemistry = 89.7843 % +percentage of rho/U/Y/E = 4.29211 % +========Time details of each equation======= +rhoEqn Time = 0.00031 s +rhoEqn assamble = 0.000247 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001091 s +UEqn assamble = 0.000663 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000428 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.0015 s +YEqn assamble = 0.000539 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000104 s +YEqn correct boundary = 0 s +EEqn Time = 0.000368 s +EEqn assamble = 0.000276 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 139.82 s ClockTime = 140 s +Courant Number mean: 0.0105429 max: 0.0361234 +Time = 0.0013075 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22573 + Current mass in system = 1.60475e-09 + Linear momentum = (2.54841e-11 -1.17525e-08 0) + |Linear momentum| = 1.17525e-08 + Linear kinetic energy = 4.45618e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 382.973, 540.2 + Mass transfer phase change = 1.01397e-10 + D10, D32, Dmax (mu) = 59.3715, 87.4747, 155.124 + Liquid penetration 95% mass (m) = 0.00942529 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00910298, Final residual = 1.26125e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00292345, Final residual = 9.25916e-07, No Iterations 1 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00178475, Final residual = 2.28653e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00254488, Final residual = 3.6503e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00260801, Final residual = 3.89183e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0026084, Final residual = 3.89612e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00374556, Final residual = 3.5068e-07, No Iterations 1 +min/max(T) = 699.124, 2714.64 +GAMG: Solving for p, Initial residual = 0.39037, Final residual = 0.00238262, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.68457e-06, global = 6.46209e-06, cumulative = 0.0023192 +GAMG: Solving for p, Initial residual = 0.00281106, Final residual = 2.91981e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.51287e-06, global = 6.51276e-06, cumulative = 0.00232571 +smoothSolver: Solving for epsilon, Initial residual = 0.00113774, Final residual = 3.06697e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00185982, Final residual = 7.11064e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100465 s +other Time = 1e-06 s +rho Equations = 0.000208 s +U Equations = 0.00126 s +Y Equations = 0.00257965 s +E Equations = 0.000602 s +p Equations = 0.002253 s +calculate parcels = 91.3603 s +chemistry correctThermo = 0.002534 s +turbulence correct = 0.000847 s +combustion correct(in Y) = 0.0899634 s +percentage of chemistry = 89.547 % +percentage of rho/U/Y/E = 4.62812 % +========Time details of each equation======= +rhoEqn Time = 0.00034 s +rhoEqn assamble = 0.000271 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00126 s +UEqn assamble = 0.000761 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000499 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001744 s +YEqn assamble = 0.000641 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.9e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000443 s +EEqn assamble = 0.000327 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 140.29 s ClockTime = 141 s +Courant Number mean: 0.0105171 max: 0.0360766 +Time = 0.00131 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22573 + Current mass in system = 1.6042e-09 + Linear momentum = (2.4942e-11 -1.17399e-08 0) + |Linear momentum| = 1.17399e-08 + Linear kinetic energy = 4.44812e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 383.107, 540.2 + Mass transfer phase change = 1.01943e-10 + D10, D32, Dmax (mu) = 59.3095, 87.5122, 155.211 + Liquid penetration 95% mass (m) = 0.00944359 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00776891, Final residual = 1.0596e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0030861, Final residual = 9.67154e-07, No Iterations 1 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00168924, Final residual = 2.08689e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00250588, Final residual = 3.55231e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00257221, Final residual = 3.80343e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0025726, Final residual = 3.80785e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00370067, Final residual = 3.40701e-07, No Iterations 1 +min/max(T) = 700.586, 2722 +GAMG: Solving for p, Initial residual = 0.345503, Final residual = 0.00202132, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.52173e-06, global = 6.2274e-06, cumulative = 0.00233194 +GAMG: Solving for p, Initial residual = 0.00210013, Final residual = 9.19492e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.29025e-06, global = 6.28975e-06, cumulative = 0.00233823 +smoothSolver: Solving for epsilon, Initial residual = 0.00111632, Final residual = 2.99824e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.001831, Final residual = 6.97439e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103631 s +other Time = 1e-06 s +rho Equations = 0.000178 s +U Equations = 0.001135 s +Y Equations = 0.00213719 s +E Equations = 0.000486 s +p Equations = 0.00192 s +calculate parcels = 91.7383 s +chemistry correctThermo = 0.002065 s +turbulence correct = 0.000816 s +combustion correct(in Y) = 0.0946938 s +percentage of chemistry = 91.3759 % +percentage of rho/U/Y/E = 3.79828 % +========Time details of each equation======= +rhoEqn Time = 0.000292 s +rhoEqn assamble = 0.000231 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001134 s +UEqn assamble = 0.000697 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000437 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001502 s +YEqn assamble = 0.000522 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000123 s +YEqn correct boundary = 0 s +EEqn Time = 0.000369 s +EEqn assamble = 0.000275 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 140.77 s ClockTime = 141 s +Courant Number mean: 0.0104922 max: 0.0355541 +Time = 0.0013125 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22567 + Current mass in system = 1.6035e-09 + Linear momentum = (2.43265e-11 -1.17262e-08 0) + |Linear momentum| = 1.17262e-08 + Linear kinetic energy = 4.43969e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 383.242, 540.2 + Mass transfer phase change = 1.02642e-10 + D10, D32, Dmax (mu) = 60.2363, 87.5879, 155.3 + Liquid penetration 95% mass (m) = 0.00946236 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00606014, Final residual = 8.89288e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00325045, Final residual = 4.04356e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0022157, Final residual = 3.39572e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00248076, Final residual = 3.50149e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00250747, Final residual = 3.74611e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00250787, Final residual = 3.75022e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00375327, Final residual = 3.53607e-07, No Iterations 1 +min/max(T) = 702.073, 2728.97 +GAMG: Solving for p, Initial residual = 0.292018, Final residual = 0.00317472, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.27793e-06, global = 7.62834e-06, cumulative = 0.00234586 +GAMG: Solving for p, Initial residual = 0.00308544, Final residual = 5.51478e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.06311e-06, global = 8.06289e-06, cumulative = 0.00235392 +smoothSolver: Solving for epsilon, Initial residual = 0.00111542, Final residual = 2.90041e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00180729, Final residual = 6.76674e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09609 s +other Time = 0 s +rho Equations = 0.00015 s +U Equations = 0.000992 s +Y Equations = 0.00244254 s +E Equations = 0.000608 s +p Equations = 0.002731 s +calculate parcels = 92.1059 s +chemistry correctThermo = 0.002864 s +turbulence correct = 0.000972 s +combustion correct(in Y) = 0.0850935 s +percentage of chemistry = 88.556 % +percentage of rho/U/Y/E = 4.36313 % +========Time details of each equation======= +rhoEqn Time = 0.000297 s +rhoEqn assamble = 0.000235 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000991 s +UEqn assamble = 0.000575 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000416 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001857 s +YEqn assamble = 0.000641 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000227 s +YEqn correct boundary = 0 s +EEqn Time = 0.000451 s +EEqn assamble = 0.000338 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 141.23 s ClockTime = 142 s +Courant Number mean: 0.010445 max: 0.0348991 +Time = 0.001315 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22565 + Current mass in system = 1.60285e-09 + Linear momentum = (2.40468e-11 -1.17123e-08 0) + |Linear momentum| = 1.17123e-08 + Linear kinetic energy = 4.43095e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 383.376, 540.2 + Mass transfer phase change = 1.03289e-10 + D10, D32, Dmax (mu) = 60.207, 87.641, 155.387 + Liquid penetration 95% mass (m) = 0.00948132 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0108426, Final residual = 1.54713e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00380364, Final residual = 4.81455e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00197147, Final residual = 3.02693e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00240798, Final residual = 3.3846e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00244611, Final residual = 3.60428e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00244647, Final residual = 3.60813e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00370023, Final residual = 3.43966e-07, No Iterations 1 +min/max(T) = 703.558, 2735.6 +GAMG: Solving for p, Initial residual = 0.249547, Final residual = 0.00339728, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.44477e-06, global = 7.1513e-06, cumulative = 0.00236107 +GAMG: Solving for p, Initial residual = 0.00319845, Final residual = 3.97686e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.44873e-06, global = 7.44843e-06, cumulative = 0.00236852 +smoothSolver: Solving for epsilon, Initial residual = 0.00106408, Final residual = 2.74796e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00174888, Final residual = 6.48202e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095402 s +other Time = 1e-06 s +rho Equations = 0.000275 s +U Equations = 0.001487 s +Y Equations = 0.00234491 s +E Equations = 0.000496 s +p Equations = 0.002265 s +calculate parcels = 92.4727 s +chemistry correctThermo = 0.002086 s +turbulence correct = 0.000878 s +combustion correct(in Y) = 0.0852741 s +percentage of chemistry = 89.384 % +percentage of rho/U/Y/E = 4.82475 % +========Time details of each equation======= +rhoEqn Time = 0.000398 s +rhoEqn assamble = 0.000318 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001485 s +UEqn assamble = 0.000938 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000547 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001522 s +YEqn assamble = 0.000543 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 3.8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000368 s +EEqn assamble = 0.000275 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 141.7 s ClockTime = 142 s +Courant Number mean: 0.0103979 max: 0.0348782 +Time = 0.0013175 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22561 + Current mass in system = 1.60222e-09 + Linear momentum = (2.40108e-11 -1.16982e-08 0) + |Linear momentum| = 1.16982e-08 + Linear kinetic energy = 4.42204e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 383.512, 540.2 + Mass transfer phase change = 1.03926e-10 + D10, D32, Dmax (mu) = 60.4372, 87.705, 155.473 + Liquid penetration 95% mass (m) = 0.00950038 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0115668, Final residual = 1.6097e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00426712, Final residual = 5.34219e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00187666, Final residual = 2.44393e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00235795, Final residual = 3.25792e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00239781, Final residual = 3.43812e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00239816, Final residual = 3.44187e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00362627, Final residual = 3.30917e-07, No Iterations 1 +min/max(T) = 705.056, 2741.97 +GAMG: Solving for p, Initial residual = 0.209218, Final residual = 0.00287263, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.01397e-05, global = 7.00082e-06, cumulative = 0.00237552 +GAMG: Solving for p, Initial residual = 0.00273142, Final residual = 6.84382e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.34225e-06, global = 7.3415e-06, cumulative = 0.00238286 +smoothSolver: Solving for epsilon, Initial residual = 0.00103423, Final residual = 2.65221e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00169947, Final residual = 6.24311e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.098 s +other Time = 0 s +rho Equations = 0.000171 s +U Equations = 0.001102 s +Y Equations = 0.00241774 s +E Equations = 0.000596 s +p Equations = 0.002559 s +calculate parcels = 92.7595 s +chemistry correctThermo = 0.00288 s +turbulence correct = 0.000967 s +combustion correct(in Y) = 0.0871183 s +percentage of chemistry = 88.8962 % +percentage of rho/U/Y/E = 4.37422 % +========Time details of each equation======= +rhoEqn Time = 0.000317 s +rhoEqn assamble = 0.000248 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001101 s +UEqn assamble = 0.000685 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000416 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001867 s +YEqn assamble = 0.000626 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000255 s +YEqn correct boundary = 0 s +EEqn Time = 0.000441 s +EEqn assamble = 0.000327 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 142.08 s ClockTime = 143 s +Courant Number mean: 0.0103501 max: 0.0346703 +Time = 0.00132 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22559 + Current mass in system = 1.60159e-09 + Linear momentum = (2.38311e-11 -1.16839e-08 0) + |Linear momentum| = 1.16839e-08 + Linear kinetic energy = 4.41293e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 383.648, 540.2 + Mass transfer phase change = 1.04551e-10 + D10, D32, Dmax (mu) = 60.4733, 87.76, 155.562 + Liquid penetration 95% mass (m) = 0.00951871 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0111119, Final residual = 1.57128e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00458528, Final residual = 5.73904e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00182468, Final residual = 2.25014e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00232429, Final residual = 3.12601e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00236597, Final residual = 3.31561e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00236632, Final residual = 3.31924e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0035942, Final residual = 3.22568e-07, No Iterations 1 +min/max(T) = 706.62, 2748.06 +GAMG: Solving for p, Initial residual = 0.179162, Final residual = 0.00178962, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.35537e-06, global = 7.16544e-06, cumulative = 0.00239003 +GAMG: Solving for p, Initial residual = 0.00167466, Final residual = 8.36419e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.21167e-06, global = 7.2107e-06, cumulative = 0.00239724 +smoothSolver: Solving for epsilon, Initial residual = 0.00103195, Final residual = 2.62443e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00168181, Final residual = 6.12452e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.101515 s +other Time = 0 s +rho Equations = 0.000182 s +U Equations = 0.001302 s +Y Equations = 0.002525 s +E Equations = 0.000594 s +p Equations = 0.002359 s +calculate parcels = 93.1212 s +chemistry correctThermo = 0.002864 s +turbulence correct = 0.000963 s +combustion correct(in Y) = 0.090524 s +percentage of chemistry = 89.173 % +percentage of rho/U/Y/E = 4.53431 % +========Time details of each equation======= +rhoEqn Time = 0.00032 s +rhoEqn assamble = 0.000252 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001302 s +UEqn assamble = 0.000795 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000507 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001862 s +YEqn assamble = 0.00065 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000192 s +YEqn correct boundary = 0 s +EEqn Time = 0.000439 s +EEqn assamble = 0.000327 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 142.54 s ClockTime = 143 s +Courant Number mean: 0.0103051 max: 0.0345122 +Time = 0.0013225 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22555 + Current mass in system = 1.60089e-09 + Linear momentum = (2.35229e-11 -1.16687e-08 0) + |Linear momentum| = 1.16688e-08 + Linear kinetic energy = 4.40347e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 383.785, 540.2 + Mass transfer phase change = 1.05257e-10 + D10, D32, Dmax (mu) = 60.6188, 87.832, 155.652 + Liquid penetration 95% mass (m) = 0.00953745 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.010137, Final residual = 1.3972e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00495163, Final residual = 6.10936e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00210586, Final residual = 2.72103e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00230065, Final residual = 3.05879e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00232021, Final residual = 3.23947e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00232056, Final residual = 3.24304e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00361348, Final residual = 3.20603e-07, No Iterations 1 +min/max(T) = 708.27, 2753.64 +GAMG: Solving for p, Initial residual = 0.155008, Final residual = 0.00174983, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.46136e-06, global = 7.79534e-06, cumulative = 0.00240503 +GAMG: Solving for p, Initial residual = 0.00160867, Final residual = 2.58841e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.13556e-06, global = 8.13537e-06, cumulative = 0.00241317 +smoothSolver: Solving for epsilon, Initial residual = 0.00101056, Final residual = 2.53475e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00165252, Final residual = 5.96315e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.104612 s +other Time = 0 s +rho Equations = 0.000158 s +U Equations = 0.001008 s +Y Equations = 0.00200281 s +E Equations = 0.00055 s +p Equations = 0.002147 s +calculate parcels = 93.4795 s +chemistry correctThermo = 0.002032 s +turbulence correct = 0.000803 s +combustion correct(in Y) = 0.0957412 s +percentage of chemistry = 91.5203 % +percentage of rho/U/Y/E = 3.55486 % +========Time details of each equation======= +rhoEqn Time = 0.000282 s +rhoEqn assamble = 0.000221 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001008 s +UEqn assamble = 0.00058 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000428 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001436 s +YEqn assamble = 0.000505 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000126 s +YEqn correct boundary = 0 s +EEqn Time = 0.000435 s +EEqn assamble = 0.000339 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 143.01 s ClockTime = 144 s +Courant Number mean: 0.0102438 max: 0.0344667 +Time = 0.001325 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22548 + Current mass in system = 1.60008e-09 + Linear momentum = (2.32688e-11 -1.16527e-08 0) + |Linear momentum| = 1.16527e-08 + Linear kinetic energy = 4.39358e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 383.924, 540.2 + Mass transfer phase change = 1.06067e-10 + D10, D32, Dmax (mu) = 61.0646, 87.9133, 155.74 + Liquid penetration 95% mass (m) = 0.00955588 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0115435, Final residual = 1.42568e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00562801, Final residual = 6.67539e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00244207, Final residual = 3.46862e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00226291, Final residual = 2.96622e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00226933, Final residual = 3.17103e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00226968, Final residual = 3.17496e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00362939, Final residual = 3.24939e-07, No Iterations 1 +min/max(T) = 709.952, 2758.79 +GAMG: Solving for p, Initial residual = 0.137591, Final residual = 0.00182375, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.10941e-05, global = 8.69403e-06, cumulative = 0.00242186 +GAMG: Solving for p, Initial residual = 0.00169146, Final residual = 4.12328e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.33607e-06, global = 9.33545e-06, cumulative = 0.0024312 +smoothSolver: Solving for epsilon, Initial residual = 0.000994351, Final residual = 2.45468e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0016184, Final residual = 5.7786e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.104919 s +other Time = 1e-06 s +rho Equations = 0.00024 s +U Equations = 0.001702 s +Y Equations = 0.0023713 s +E Equations = 0.000494 s +p Equations = 0.002148 s +calculate parcels = 93.8323 s +chemistry correctThermo = 0.002027 s +turbulence correct = 0.000811 s +combustion correct(in Y) = 0.0948437 s +percentage of chemistry = 90.3971 % +percentage of rho/U/Y/E = 4.58192 % +========Time details of each equation======= +rhoEqn Time = 0.000359 s +rhoEqn assamble = 0.000278 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001702 s +UEqn assamble = 0.000864 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000838 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001291 s +YEqn assamble = 0.000549 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -0.00011 s +YEqn correct boundary = 0 s +EEqn Time = 0.000378 s +EEqn assamble = 0.00028 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 143.47 s ClockTime = 144 s +Courant Number mean: 0.0101593 max: 0.0341856 +Time = 0.0013275 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22544 + Current mass in system = 1.59934e-09 + Linear momentum = (2.23508e-11 -1.16364e-08 0) + |Linear momentum| = 1.16364e-08 + Linear kinetic energy = 4.38334e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 384.063, 540.2 + Mass transfer phase change = 1.068e-10 + D10, D32, Dmax (mu) = 61.1369, 87.986, 155.825 + Liquid penetration 95% mass (m) = 0.0095736 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0163856, Final residual = 1.77073e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00653916, Final residual = 7.37586e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00208693, Final residual = 2.63211e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0021865, Final residual = 2.80654e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00220049, Final residual = 2.94865e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00220082, Final residual = 2.95211e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00352819, Final residual = 3.01833e-07, No Iterations 1 +min/max(T) = 711.602, 2763.75 +GAMG: Solving for p, Initial residual = 0.124661, Final residual = 0.00190313, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.16763e-05, global = 8.0488e-06, cumulative = 0.00243925 +GAMG: Solving for p, Initial residual = 0.00176143, Final residual = 3.79014e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.44382e-06, global = 8.44323e-06, cumulative = 0.00244769 +smoothSolver: Solving for epsilon, Initial residual = 0.000952613, Final residual = 2.31077e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00156081, Final residual = 5.48463e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.085874 s +other Time = 0 s +rho Equations = 0.000182 s +U Equations = 0.001195 s +Y Equations = 0.00232882 s +E Equations = 0.000504 s +p Equations = 0.002095 s +calculate parcels = 94.1832 s +chemistry correctThermo = 0.002022 s +turbulence correct = 0.000877 s +combustion correct(in Y) = 0.0764452 s +percentage of chemistry = 89.0202 % +percentage of rho/U/Y/E = 4.90232 % +========Time details of each equation======= +rhoEqn Time = 0.000303 s +rhoEqn assamble = 0.000238 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001194 s +UEqn assamble = 0.000689 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000505 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001668 s +YEqn assamble = 0.000663 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000142 s +YEqn correct boundary = 0 s +EEqn Time = 0.000378 s +EEqn assamble = 0.000281 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.7e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 143.9 s ClockTime = 144 s +Courant Number mean: 0.0100818 max: 0.0337048 +Time = 0.00133 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22539 + Current mass in system = 1.5986e-09 + Linear momentum = (2.13935e-11 -1.16196e-08 0) + |Linear momentum| = 1.16196e-08 + Linear kinetic energy = 4.37275e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 384.202, 540.2 + Mass transfer phase change = 1.07543e-10 + D10, D32, Dmax (mu) = 61.5071, 88.0571, 155.915 + Liquid penetration 95% mass (m) = 0.00959327 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0155825, Final residual = 1.77787e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00717892, Final residual = 7.98378e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00215243, Final residual = 2.75215e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00214102, Final residual = 2.66931e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00215178, Final residual = 2.8244e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00215209, Final residual = 2.82772e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00347002, Final residual = 2.93562e-07, No Iterations 1 +min/max(T) = 713.32, 2768.61 +GAMG: Solving for p, Initial residual = 0.111447, Final residual = 0.00145224, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.08528e-05, global = 8.37361e-06, cumulative = 0.00245606 +GAMG: Solving for p, Initial residual = 0.00134545, Final residual = 2.48392e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.57023e-06, global = 8.56986e-06, cumulative = 0.00246463 +smoothSolver: Solving for epsilon, Initial residual = 0.000937174, Final residual = 2.20848e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00152664, Final residual = 5.26152e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.080912 s +other Time = 0 s +rho Equations = 0.000169 s +U Equations = 0.001154 s +Y Equations = 0.0021284 s +E Equations = 0.000483 s +p Equations = 0.002084 s +calculate parcels = 94.496 s +chemistry correctThermo = 0.001991 s +turbulence correct = 0.000839 s +combustion correct(in Y) = 0.0718786 s +percentage of chemistry = 88.8355 % +percentage of rho/U/Y/E = 4.86257 % +========Time details of each equation======= +rhoEqn Time = 0.000285 s +rhoEqn assamble = 0.000227 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001154 s +UEqn assamble = 0.000654 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.0005 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001549 s +YEqn assamble = 0.000545 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000125 s +YEqn correct boundary = 0 s +EEqn Time = 0.000363 s +EEqn assamble = 0.000271 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 144.3 s ClockTime = 145 s +Courant Number mean: 0.0100042 max: 0.0332629 +Time = 0.0013325 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22536 + Current mass in system = 1.59781e-09 + Linear momentum = (2.06074e-11 -1.16021e-08 0) + |Linear momentum| = 1.16022e-08 + Linear kinetic energy = 4.36179e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 384.342, 540.2 + Mass transfer phase change = 1.08337e-10 + D10, D32, Dmax (mu) = 61.4544, 88.1207, 156 + Liquid penetration 95% mass (m) = 0.00961135 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0149728, Final residual = 1.82006e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00784357, Final residual = 8.64372e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00227185, Final residual = 2.94882e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00210353, Final residual = 2.54568e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00210411, Final residual = 2.74091e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00210443, Final residual = 2.74417e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00345867, Final residual = 2.86814e-07, No Iterations 1 +min/max(T) = 715.184, 2772.71 +GAMG: Solving for p, Initial residual = 0.100695, Final residual = 0.001384, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.15647e-05, global = 8.89566e-06, cumulative = 0.00247353 +GAMG: Solving for p, Initial residual = 0.00128444, Final residual = 7.26751e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.152e-06, global = 9.15056e-06, cumulative = 0.00248268 +smoothSolver: Solving for epsilon, Initial residual = 0.000922457, Final residual = 2.17705e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00149776, Final residual = 5.1209e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.108672 s +other Time = 0 s +rho Equations = 0.000153 s +U Equations = 0.001317 s +Y Equations = 0.00285665 s +E Equations = 0.000606 s +p Equations = 0.00255 s +calculate parcels = 94.837 s +chemistry correctThermo = 0.002851 s +turbulence correct = 0.000972 s +combustion correct(in Y) = 0.0971343 s +percentage of chemistry = 89.3831 % +percentage of rho/U/Y/E = 4.53903 % +========Time details of each equation======= +rhoEqn Time = 0.000302 s +rhoEqn assamble = 0.00024 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001314 s +UEqn assamble = 0.000555 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000759 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001802 s +YEqn assamble = 0.000652 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -1.8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000447 s +EEqn assamble = 0.000334 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 144.75 s ClockTime = 145 s +Courant Number mean: 0.00992073 max: 0.0331691 +Time = 0.001335 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22532 + Current mass in system = 1.59707e-09 + Linear momentum = (1.9595e-11 -1.15844e-08 0) + |Linear momentum| = 1.15844e-08 + Linear kinetic energy = 4.35055e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 384.484, 540.2 + Mass transfer phase change = 1.09072e-10 + D10, D32, Dmax (mu) = 61.6453, 88.1883, 156.097 + Liquid penetration 95% mass (m) = 0.00963008 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0143226, Final residual = 1.79641e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0084137, Final residual = 9.13414e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00203528, Final residual = 2.18586e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00205317, Final residual = 2.45402e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00206262, Final residual = 2.60691e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00206296, Final residual = 2.61045e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00340078, Final residual = 2.74994e-07, No Iterations 1 +min/max(T) = 717.071, 2776.53 +GAMG: Solving for p, Initial residual = 0.0904753, Final residual = 0.0011371, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.08663e-05, global = 8.51778e-06, cumulative = 0.0024912 +GAMG: Solving for p, Initial residual = 0.00106708, Final residual = 6.63423e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.47796e-06, global = 8.47649e-06, cumulative = 0.00249967 +smoothSolver: Solving for epsilon, Initial residual = 0.000893323, Final residual = 2.06648e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00146898, Final residual = 4.92969e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.109502 s +other Time = 0 s +rho Equations = 0.000155 s +U Equations = 0.00127 s +Y Equations = 0.00239069 s +E Equations = 0.000627 s +p Equations = 0.002376 s +calculate parcels = 95.1829 s +chemistry correctThermo = 0.00282 s +turbulence correct = 0.001011 s +combustion correct(in Y) = 0.0986503 s +percentage of chemistry = 90.09 % +percentage of rho/U/Y/E = 4.05718 % +========Time details of each equation======= +rhoEqn Time = 0.0003 s +rhoEqn assamble = 0.000234 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00127 s +UEqn assamble = 0.000769 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000501 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001758 s +YEqn assamble = 0.000616 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000179 s +YEqn correct boundary = 0 s +EEqn Time = 0.000471 s +EEqn assamble = 0.000355 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 145.2 s ClockTime = 146 s +Courant Number mean: 0.00983195 max: 0.0329633 +Time = 0.0013375 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22528 + Current mass in system = 1.59628e-09 + Linear momentum = (1.87914e-11 -1.15661e-08 0) + |Linear momentum| = 1.15661e-08 + Linear kinetic energy = 4.33904e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 384.624, 540.2 + Mass transfer phase change = 1.0986e-10 + D10, D32, Dmax (mu) = 61.7972, 88.2613, 156.202 + Liquid penetration 95% mass (m) = 0.00964909 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.012622, Final residual = 1.60661e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00911614, Final residual = 9.57568e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00218879, Final residual = 2.27917e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00204101, Final residual = 2.36983e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00203756, Final residual = 2.51573e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00203789, Final residual = 2.51925e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.003394, Final residual = 2.69745e-07, No Iterations 1 +min/max(T) = 718.941, 2780.2 +GAMG: Solving for p, Initial residual = 0.0806007, Final residual = 0.000906444, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.07123e-05, global = 8.92711e-06, cumulative = 0.0025086 +GAMG: Solving for p, Initial residual = 0.000851027, Final residual = 3.4455e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.07734e-06, global = 9.07673e-06, cumulative = 0.00251768 +smoothSolver: Solving for epsilon, Initial residual = 0.000879537, Final residual = 2.00912e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00143985, Final residual = 4.79039e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103424 s +other Time = 1e-06 s +rho Equations = 0.000151 s +U Equations = 0.001123 s +Y Equations = 0.00363021 s +E Equations = 0.001031 s +p Equations = 0.00209 s +calculate parcels = 95.5433 s +chemistry correctThermo = 0.002626 s +turbulence correct = 0.00084 s +combustion correct(in Y) = 0.0917368 s +percentage of chemistry = 88.6997 % +percentage of rho/U/Y/E = 5.73872 % +========Time details of each equation======= +rhoEqn Time = 0.000272 s +rhoEqn assamble = 0.000215 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001121 s +UEqn assamble = 0.000663 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000458 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.003051 s +YEqn assamble = 0.000989 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000558 s +YEqn correct boundary = 0 s +EEqn Time = 0.000749 s +EEqn assamble = 0.000548 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000201 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 145.67 s ClockTime = 146 s +Courant Number mean: 0.00974122 max: 0.0325786 +Time = 0.00134 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22528 + Current mass in system = 1.5956e-09 + Linear momentum = (1.82883e-11 -1.15479e-08 0) + |Linear momentum| = 1.1548e-08 + Linear kinetic energy = 4.32738e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 384.765, 540.2 + Mass transfer phase change = 1.10542e-10 + D10, D32, Dmax (mu) = 61.7169, 88.306, 156.302 + Liquid penetration 95% mass (m) = 0.00966865 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0107449, Final residual = 1.4387e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00987971, Final residual = 1.01002e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00186005, Final residual = 1.95472e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00199671, Final residual = 2.30749e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00201724, Final residual = 2.48454e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00201757, Final residual = 2.48813e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00330643, Final residual = 2.63488e-07, No Iterations 1 +min/max(T) = 720.827, 2783.54 +GAMG: Solving for p, Initial residual = 0.0728662, Final residual = 0.000790978, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.89533e-06, global = 7.65798e-06, cumulative = 0.00252533 +GAMG: Solving for p, Initial residual = 0.000745073, Final residual = 3.09175e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.8585e-06, global = 7.85763e-06, cumulative = 0.00253319 +smoothSolver: Solving for epsilon, Initial residual = 0.000873623, Final residual = 1.96556e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00142881, Final residual = 4.67174e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.104762 s +other Time = 0 s +rho Equations = 0.000185 s +U Equations = 0.001309 s +Y Equations = 0.00212192 s +E Equations = 0.000494 s +p Equations = 0.002399 s +calculate parcels = 95.9094 s +chemistry correctThermo = 0.002778 s +turbulence correct = 0.000959 s +combustion correct(in Y) = 0.0942721 s +percentage of chemistry = 89.9869 % +percentage of rho/U/Y/E = 3.9231 % +========Time details of each equation======= +rhoEqn Time = 0.00033 s +rhoEqn assamble = 0.000263 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001308 s +UEqn assamble = 0.000799 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000509 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001453 s +YEqn assamble = 0.000522 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.9e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000373 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 146.14 s ClockTime = 147 s +Courant Number mean: 0.00965621 max: 0.0321899 +Time = 0.0013425 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22526 + Current mass in system = 1.59485e-09 + Linear momentum = (1.8015e-11 -1.15291e-08 0) + |Linear momentum| = 1.15291e-08 + Linear kinetic energy = 4.31544e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 384.904, 540.2 + Mass transfer phase change = 1.11288e-10 + D10, D32, Dmax (mu) = 61.7276, 88.3665, 156.387 + Liquid penetration 95% mass (m) = 0.00968844 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00886657, Final residual = 1.19001e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.010578, Final residual = 1.03854e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00204833, Final residual = 2.33018e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00197795, Final residual = 2.25519e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00198239, Final residual = 2.40417e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00198273, Final residual = 2.40757e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00327687, Final residual = 2.60131e-07, No Iterations 1 +min/max(T) = 722.908, 2786.45 +GAMG: Solving for p, Initial residual = 0.066259, Final residual = 0.000739188, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.01525e-05, global = 8.20368e-06, cumulative = 0.0025414 +GAMG: Solving for p, Initial residual = 0.000685141, Final residual = 3.88257e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.60443e-06, global = 8.60384e-06, cumulative = 0.00255 +smoothSolver: Solving for epsilon, Initial residual = 0.000875949, Final residual = 1.96673e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00143286, Final residual = 4.65395e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.076486 s +other Time = 1e-06 s +rho Equations = 0.000171 s +U Equations = 0.001083 s +Y Equations = 0.00217887 s +E Equations = 0.000587 s +p Equations = 0.001967 s +calculate parcels = 96.268 s +chemistry correctThermo = 0.002029 s +turbulence correct = 0.000805 s +combustion correct(in Y) = 0.0674771 s +percentage of chemistry = 88.2215 % +percentage of rho/U/Y/E = 5.25569 % +========Time details of each equation======= +rhoEqn Time = 0.000289 s +rhoEqn assamble = 0.000229 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001081 s +UEqn assamble = 0.000594 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000487 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001575 s +YEqn assamble = 0.000543 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00013 s +YEqn correct boundary = 0 s +EEqn Time = 0.000425 s +EEqn assamble = 0.000326 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 146.57 s ClockTime = 147 s +Courant Number mean: 0.00956604 max: 0.0320696 +Time = 0.001345 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22520 + Current mass in system = 1.59399e-09 + Linear momentum = (1.79049e-11 -1.15094e-08 0) + |Linear momentum| = 1.15094e-08 + Linear kinetic energy = 4.30314e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 385.043, 540.2 + Mass transfer phase change = 1.12151e-10 + D10, D32, Dmax (mu) = 61.9445, 88.4515, 156.472 + Liquid penetration 95% mass (m) = 0.00970951 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00815745, Final residual = 9.43596e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0112732, Final residual = 1.06141e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00232671, Final residual = 2.59065e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00196267, Final residual = 2.21846e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00194078, Final residual = 2.33472e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0019411, Final residual = 2.33796e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00329044, Final residual = 2.59894e-07, No Iterations 1 +min/max(T) = 725.097, 2789.1 +GAMG: Solving for p, Initial residual = 0.0612468, Final residual = 0.000751235, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.13502e-05, global = 9.54359e-06, cumulative = 0.00255954 +GAMG: Solving for p, Initial residual = 0.000701021, Final residual = 4.46789e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.94711e-06, global = 9.94613e-06, cumulative = 0.00256949 +smoothSolver: Solving for epsilon, Initial residual = 0.000856356, Final residual = 1.90644e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0014175, Final residual = 4.57665e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.10839 s +other Time = 0 s +rho Equations = 0.000173 s +U Equations = 0.001166 s +Y Equations = 0.00246684 s +E Equations = 0.000592 s +p Equations = 0.00243 s +calculate parcels = 96.5396 s +chemistry correctThermo = 0.002901 s +turbulence correct = 0.00098 s +combustion correct(in Y) = 0.0974782 s +percentage of chemistry = 89.9328 % +percentage of rho/U/Y/E = 4.05742 % +========Time details of each equation======= +rhoEqn Time = 0.000318 s +rhoEqn assamble = 0.000253 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001165 s +UEqn assamble = 0.000669 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000496 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001827 s +YEqn assamble = 0.000631 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000198 s +YEqn correct boundary = 0 s +EEqn Time = 0.000434 s +EEqn assamble = 0.000323 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 146.95 s ClockTime = 147 s +Courant Number mean: 0.00945929 max: 0.0320533 +Time = 0.0013475 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22515 + Current mass in system = 1.59299e-09 + Linear momentum = (1.81092e-11 -1.14883e-08 0) + |Linear momentum| = 1.14883e-08 + Linear kinetic energy = 4.29012e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 385.179, 540.2 + Mass transfer phase change = 1.13151e-10 + D10, D32, Dmax (mu) = 61.9488, 88.5313, 156.556 + Liquid penetration 95% mass (m) = 0.00972911 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0108225, Final residual = 1.05668e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0122688, Final residual = 1.10393e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0027337, Final residual = 3.49152e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00192331, Final residual = 2.18883e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00189391, Final residual = 2.33855e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00189425, Final residual = 2.34175e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00331216, Final residual = 2.6217e-07, No Iterations 1 +min/max(T) = 727.199, 2791.74 +GAMG: Solving for p, Initial residual = 0.0584228, Final residual = 0.00138074, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.48432e-05, global = 1.00414e-05, cumulative = 0.00257953 +GAMG: Solving for p, Initial residual = 0.00130053, Final residual = 8.01357e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.15245e-05, global = 1.15215e-05, cumulative = 0.00259105 +smoothSolver: Solving for epsilon, Initial residual = 0.000875149, Final residual = 1.893e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00140907, Final residual = 4.49994e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.099225 s +other Time = 0 s +rho Equations = 0.000238 s +U Equations = 0.001465 s +Y Equations = 0.00256442 s +E Equations = 0.000589 s +p Equations = 0.002417 s +calculate parcels = 96.8826 s +chemistry correctThermo = 0.002825 s +turbulence correct = 0.001008 s +combustion correct(in Y) = 0.0878786 s +percentage of chemistry = 88.565 % +percentage of rho/U/Y/E = 4.89436 % +========Time details of each equation======= +rhoEqn Time = 0.000382 s +rhoEqn assamble = 0.000305 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001464 s +UEqn assamble = 0.000912 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000552 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001948 s +YEqn assamble = 0.000658 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000211 s +YEqn correct boundary = 0 s +EEqn Time = 0.000435 s +EEqn assamble = 0.000323 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 147.39 s ClockTime = 148 s +Courant Number mean: 0.00933485 max: 0.0311833 +Time = 0.00135 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22514 + Current mass in system = 1.5922e-09 + Linear momentum = (1.81219e-11 -1.14664e-08 0) + |Linear momentum| = 1.14664e-08 + Linear kinetic energy = 4.27627e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 385.315, 540.2 + Mass transfer phase change = 1.13948e-10 + D10, D32, Dmax (mu) = 61.8672, 88.576, 156.645 + Liquid penetration 95% mass (m) = 0.00974896 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0156906, Final residual = 1.41814e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0137511, Final residual = 1.21345e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00203837, Final residual = 2.15632e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00182764, Final residual = 2.06915e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00182423, Final residual = 2.20798e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00182456, Final residual = 2.21089e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0031667, Final residual = 2.49413e-07, No Iterations 1 +min/max(T) = 728.21, 2794.74 +GAMG: Solving for p, Initial residual = 0.0557774, Final residual = 0.0012721, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.34751e-05, global = 8.73278e-06, cumulative = 0.00259979 +GAMG: Solving for p, Initial residual = 0.0011704, Final residual = 6.36208e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.187e-06, global = 9.18467e-06, cumulative = 0.00260897 +smoothSolver: Solving for epsilon, Initial residual = 0.000834566, Final residual = 1.79202e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00136576, Final residual = 4.28515e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.110016 s +other Time = 1e-06 s +rho Equations = 0.000148 s +U Equations = 0.001716 s +Y Equations = 0.00239619 s +E Equations = 0.000615 s +p Equations = 0.002372 s +calculate parcels = 97.2343 s +chemistry correctThermo = 0.002871 s +turbulence correct = 0.000986 s +combustion correct(in Y) = 0.0987358 s +percentage of chemistry = 89.7468 % +percentage of rho/U/Y/E = 4.43135 % +========Time details of each equation======= +rhoEqn Time = 0.000292 s +rhoEqn assamble = 0.000228 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001714 s +UEqn assamble = 0.000951 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000763 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001819 s +YEqn assamble = 0.00063 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000215 s +YEqn correct boundary = 0 s +EEqn Time = 0.000452 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 147.86 s ClockTime = 148 s +Courant Number mean: 0.00921801 max: 0.0304164 +Time = 0.0013525 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22512 + Current mass in system = 1.59143e-09 + Linear momentum = (1.79566e-11 -1.14442e-08 0) + |Linear momentum| = 1.14442e-08 + Linear kinetic energy = 4.26204e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 385.45, 540.2 + Mass transfer phase change = 1.14709e-10 + D10, D32, Dmax (mu) = 62.0164, 88.6188, 156.738 + Liquid penetration 95% mass (m) = 0.00976839 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0149514, Final residual = 1.66503e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0143316, Final residual = 1.2618e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00196166, Final residual = 1.86256e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00180385, Final residual = 1.9515e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00180812, Final residual = 2.11074e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00180844, Final residual = 2.11403e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00305941, Final residual = 2.25558e-07, No Iterations 1 +min/max(T) = 727.624, 2797.5 +GAMG: Solving for p, Initial residual = 0.0507783, Final residual = 0.0010409, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.28025e-05, global = 7.91409e-06, cumulative = 0.00261688 +GAMG: Solving for p, Initial residual = 0.000974781, Final residual = 6.26937e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 8.78206e-06, global = 8.78012e-06, cumulative = 0.00262566 +smoothSolver: Solving for epsilon, Initial residual = 0.000838104, Final residual = 1.75645e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00136659, Final residual = 4.19922e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.105362 s +other Time = 0 s +rho Equations = 0.00018 s +U Equations = 0.00128 s +Y Equations = 0.00212357 s +E Equations = 0.000488 s +p Equations = 0.001887 s +calculate parcels = 97.5849 s +chemistry correctThermo = 0.002036 s +turbulence correct = 0.000793 s +combustion correct(in Y) = 0.0963444 s +percentage of chemistry = 91.4413 % +percentage of rho/U/Y/E = 3.86436 % +========Time details of each equation======= +rhoEqn Time = 0.000297 s +rhoEqn assamble = 0.000236 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001278 s +UEqn assamble = 0.000781 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000497 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00147 s +YEqn assamble = 0.000535 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.9e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.00037 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 148.31 s ClockTime = 149 s +Courant Number mean: 0.00910638 max: 0.0305407 +Time = 0.001355 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22511 + Current mass in system = 1.59062e-09 + Linear momentum = (1.77664e-11 -1.14217e-08 0) + |Linear momentum| = 1.14217e-08 + Linear kinetic energy = 4.24767e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 385.584, 540.2 + Mass transfer phase change = 1.15523e-10 + D10, D32, Dmax (mu) = 61.9652, 88.6634, 156.834 + Liquid penetration 95% mass (m) = 0.00978874 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0154009, Final residual = 1.67611e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.015123, Final residual = 1.3155e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00208891, Final residual = 2.06034e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.001803, Final residual = 1.90915e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00179424, Final residual = 2.06703e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00179457, Final residual = 2.0703e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00304779, Final residual = 2.18938e-07, No Iterations 1 +min/max(T) = 727.191, 2799.38 +GAMG: Solving for p, Initial residual = 0.0467443, Final residual = 0.000754994, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.19009e-05, global = 9.30521e-06, cumulative = 0.00263497 +GAMG: Solving for p, Initial residual = 0.000692147, Final residual = 5.19495e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.37754e-06, global = 9.37626e-06, cumulative = 0.00264435 +smoothSolver: Solving for epsilon, Initial residual = 0.000848458, Final residual = 1.79784e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00137537, Final residual = 4.24078e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.098348 s +other Time = 1e-06 s +rho Equations = 0.000169 s +U Equations = 0.001277 s +Y Equations = 0.00244582 s +E Equations = 0.000599 s +p Equations = 0.002443 s +calculate parcels = 97.9563 s +chemistry correctThermo = 0.002827 s +turbulence correct = 0.000807 s +combustion correct(in Y) = 0.0875542 s +percentage of chemistry = 89.0249 % +percentage of rho/U/Y/E = 4.56625 % +========Time details of each equation======= +rhoEqn Time = 0.000305 s +rhoEqn assamble = 0.000242 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001275 s +UEqn assamble = 0.000788 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000487 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00182 s +YEqn assamble = 0.000646 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000199 s +YEqn correct boundary = 0 s +EEqn Time = 0.000445 s +EEqn assamble = 0.000333 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 148.78 s ClockTime = 149 s +Courant Number mean: 0.00899114 max: 0.0311642 +Time = 0.0013575 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22507 + Current mass in system = 1.58972e-09 + Linear momentum = (1.79392e-11 -1.1398e-08 0) + |Linear momentum| = 1.1398e-08 + Linear kinetic energy = 4.23277e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 385.719, 540.2 + Mass transfer phase change = 1.16427e-10 + D10, D32, Dmax (mu) = 62.0653, 88.7246, 156.934 + Liquid penetration 95% mass (m) = 0.00980874 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0150537, Final residual = 1.39121e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0157899, Final residual = 1.32085e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00232844, Final residual = 2.56202e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00179172, Final residual = 1.9292e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00176267, Final residual = 2.04231e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00176299, Final residual = 2.04549e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00305755, Final residual = 2.30075e-07, No Iterations 1 +min/max(T) = 726.854, 2800.75 +GAMG: Solving for p, Initial residual = 0.0437535, Final residual = 0.000898005, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.30849e-05, global = 9.70927e-06, cumulative = 0.00265406 +GAMG: Solving for p, Initial residual = 0.00083463, Final residual = 7.39653e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.04214e-05, global = 1.04188e-05, cumulative = 0.00266447 +smoothSolver: Solving for epsilon, Initial residual = 0.000833441, Final residual = 1.74791e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00138048, Final residual = 4.24197e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.076876 s +other Time = 0 s +rho Equations = 0.000182 s +U Equations = 0.001229 s +Y Equations = 0.0022647 s +E Equations = 0.000501 s +p Equations = 0.002034 s +calculate parcels = 98.2431 s +chemistry correctThermo = 0.001998 s +turbulence correct = 0.000937 s +combustion correct(in Y) = 0.0675303 s +percentage of chemistry = 87.8431 % +percentage of rho/U/Y/E = 5.43304 % +========Time details of each equation======= +rhoEqn Time = 0.000301 s +rhoEqn assamble = 0.000235 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001227 s +UEqn assamble = 0.000797 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00043 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00168 s +YEqn assamble = 0.00056 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00014 s +YEqn correct boundary = 0 s +EEqn Time = 0.000372 s +EEqn assamble = 0.000279 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 149.15 s ClockTime = 150 s +Courant Number mean: 0.00885382 max: 0.0318544 +Time = 0.00136 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22506 + Current mass in system = 1.58886e-09 + Linear momentum = (1.79208e-11 -1.13734e-08 0) + |Linear momentum| = 1.13735e-08 + Linear kinetic energy = 4.2172e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 385.852, 540.2 + Mass transfer phase change = 1.17285e-10 + D10, D32, Dmax (mu) = 61.9647, 88.7562, 157.034 + Liquid penetration 95% mass (m) = 0.00982849 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0154624, Final residual = 1.16237e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0168294, Final residual = 1.3347e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00219239, Final residual = 2.17505e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00175124, Final residual = 1.81213e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00174451, Final residual = 1.99567e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00174484, Final residual = 1.99888e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00298339, Final residual = 2.07882e-07, No Iterations 1 +min/max(T) = 726.456, 2802.45 +GAMG: Solving for p, Initial residual = 0.0413636, Final residual = 0.000891062, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.28468e-05, global = 9.29871e-06, cumulative = 0.00267377 +GAMG: Solving for p, Initial residual = 0.00082678, Final residual = 7.70546e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.89959e-06, global = 9.89696e-06, cumulative = 0.00268367 +smoothSolver: Solving for epsilon, Initial residual = 0.000835321, Final residual = 1.71654e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00137447, Final residual = 4.17711e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.116272 s +other Time = 0 s +rho Equations = 0.000287 s +U Equations = 0.001597 s +Y Equations = 0.00407549 s +E Equations = 0.000803 s +p Equations = 0.004368 s +calculate parcels = 98.5936 s +chemistry correctThermo = 0.002939 s +turbulence correct = 0.001406 s +combustion correct(in Y) = 0.100497 s +percentage of chemistry = 86.4323 % +percentage of rho/U/Y/E = 5.8161 % +========Time details of each equation======= +rhoEqn Time = 0.000612 s +rhoEqn assamble = 0.000466 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000146 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001596 s +UEqn assamble = 0.000999 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000597 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.003255 s +YEqn assamble = 0.00111 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00031 s +YEqn correct boundary = 0 s +EEqn Time = 0.000588 s +EEqn assamble = 0.000446 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000142 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 149.61 s ClockTime = 150 s +Courant Number mean: 0.00871789 max: 0.0323256 +Time = 0.0013625 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22505 + Current mass in system = 1.58803e-09 + Linear momentum = (1.83573e-11 -1.13476e-08 0) + |Linear momentum| = 1.13476e-08 + Linear kinetic energy = 4.20073e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 385.985, 540.2 + Mass transfer phase change = 1.18116e-10 + D10, D32, Dmax (mu) = 61.8866, 88.7787, 157.138 + Liquid penetration 95% mass (m) = 0.00984812 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0131498, Final residual = 1.02612e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0177161, Final residual = 1.3623e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00204395, Final residual = 1.91344e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00170886, Final residual = 1.81227e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00169851, Final residual = 1.96277e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00169883, Final residual = 1.96579e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00290706, Final residual = 2.07788e-07, No Iterations 1 +min/max(T) = 725.979, 2804.09 +GAMG: Solving for p, Initial residual = 0.0382049, Final residual = 0.000646564, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.20736e-05, global = 9.34049e-06, cumulative = 0.00269301 +GAMG: Solving for p, Initial residual = 0.000599576, Final residual = 4.50803e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 9.57628e-06, global = 9.57439e-06, cumulative = 0.00270258 +smoothSolver: Solving for epsilon, Initial residual = 0.000828586, Final residual = 1.6999e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00137112, Final residual = 4.13825e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.117781 s +other Time = 0 s +rho Equations = 0.000301 s +U Equations = 0.001833 s +Y Equations = 0.00323903 s +E Equations = 0.000718 s +p Equations = 0.002992 s +calculate parcels = 99.0009 s +chemistry correctThermo = 0.002896 s +turbulence correct = 0.001077 s +combustion correct(in Y) = 0.10442 s +percentage of chemistry = 88.656 % +percentage of rho/U/Y/E = 5.17149 % +========Time details of each equation======= +rhoEqn Time = 0.000477 s +rhoEqn assamble = 0.000381 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001831 s +UEqn assamble = 0.001203 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000628 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002354 s +YEqn assamble = 0.000861 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000182 s +YEqn correct boundary = 0 s +EEqn Time = 0.000506 s +EEqn assamble = 0.000383 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000123 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 150.14 s ClockTime = 151 s +Courant Number mean: 0.00858463 max: 0.0323874 +Time = 0.001365 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22499 + Current mass in system = 1.58697e-09 + Linear momentum = (1.89978e-11 -1.13199e-08 0) + |Linear momentum| = 1.13199e-08 + Linear kinetic energy = 4.18343e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 386.116, 540.2 + Mass transfer phase change = 1.19172e-10 + D10, D32, Dmax (mu) = 62.0281, 88.8285, 157.247 + Liquid penetration 95% mass (m) = 0.00986656 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0114533, Final residual = 9.96497e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0186934, Final residual = 1.41148e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00265324, Final residual = 3.02275e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00169556, Final residual = 1.78077e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00165994, Final residual = 1.95625e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00166026, Final residual = 1.9596e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00294365, Final residual = 2.1069e-07, No Iterations 1 +min/max(T) = 725.537, 2805.29 +GAMG: Solving for p, Initial residual = 0.0362406, Final residual = 0.000851513, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.46969e-05, global = 1.09182e-05, cumulative = 0.0027135 +GAMG: Solving for p, Initial residual = 0.000794903, Final residual = 6.37535e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.21672e-05, global = 1.21651e-05, cumulative = 0.00272567 +smoothSolver: Solving for epsilon, Initial residual = 0.000881993, Final residual = 1.74516e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0013993, Final residual = 4.14351e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.08065 s +other Time = 0 s +rho Equations = 0.000147 s +U Equations = 0.000986 s +Y Equations = 0.00205792 s +E Equations = 0.000489 s +p Equations = 0.001942 s +calculate parcels = 99.3504 s +chemistry correctThermo = 0.002017 s +turbulence correct = 0.00081 s +combustion correct(in Y) = 0.0720351 s +percentage of chemistry = 89.3181 % +percentage of rho/U/Y/E = 4.56282 % +========Time details of each equation======= +rhoEqn Time = 0.000267 s +rhoEqn assamble = 0.000213 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000986 s +UEqn assamble = 0.000558 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000428 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001499 s +YEqn assamble = 0.000527 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000131 s +YEqn correct boundary = 0 s +EEqn Time = 0.00037 s +EEqn assamble = 0.000276 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 150.57 s ClockTime = 151 s +Courant Number mean: 0.00843773 max: 0.0324824 +Time = 0.0013675 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22490 + Current mass in system = 1.58576e-09 + Linear momentum = (1.94885e-11 -1.12901e-08 0) + |Linear momentum| = 1.12901e-08 + Linear kinetic energy = 4.16493e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 386.247, 540.2 + Mass transfer phase change = 1.20378e-10 + D10, D32, Dmax (mu) = 62.3568, 88.8867, 157.353 + Liquid penetration 95% mass (m) = 0.00988576 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0178368, Final residual = 1.43304e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0200339, Final residual = 1.4873e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00291085, Final residual = 3.26173e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00165289, Final residual = 1.72882e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00159991, Final residual = 1.83991e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00160022, Final residual = 1.84326e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0029619, Final residual = 2.14578e-07, No Iterations 1 +min/max(T) = 725.139, 2806.76 +GAMG: Solving for p, Initial residual = 0.0350469, Final residual = 0.000863002, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.71691e-05, global = 1.25598e-05, cumulative = 0.00273823 +GAMG: Solving for p, Initial residual = 0.000820456, Final residual = 2.26758e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.39071e-05, global = 1.3906e-05, cumulative = 0.00275213 +smoothSolver: Solving for epsilon, Initial residual = 0.000891486, Final residual = 1.73809e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00140207, Final residual = 4.10382e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.110292 s +other Time = 0 s +rho Equations = 0.000176 s +U Equations = 0.001215 s +Y Equations = 0.0026485 s +E Equations = 0.000594 s +p Equations = 0.002545 s +calculate parcels = 99.7093 s +chemistry correctThermo = 0.002813 s +turbulence correct = 0.000964 s +combustion correct(in Y) = 0.0991375 s +percentage of chemistry = 89.8864 % +percentage of rho/U/Y/E = 4.20112 % +========Time details of each equation======= +rhoEqn Time = 0.000316 s +rhoEqn assamble = 0.00025 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001214 s +UEqn assamble = 0.000706 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000508 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001961 s +YEqn assamble = 0.000669 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000186 s +YEqn correct boundary = 0 s +EEqn Time = 0.000441 s +EEqn assamble = 0.000316 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000125 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 151.04 s ClockTime = 152 s +Courant Number mean: 0.00826989 max: 0.0326588 +Time = 0.00137 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22484 + Current mass in system = 1.5848e-09 + Linear momentum = (1.88391e-11 -1.12589e-08 0) + |Linear momentum| = 1.12589e-08 + Linear kinetic energy = 4.14513e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 386.374, 540.2 + Mass transfer phase change = 1.21345e-10 + D10, D32, Dmax (mu) = 62.5784, 88.9117, 157.462 + Liquid penetration 95% mass (m) = 0.00990444 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0261596, Final residual = 2.02701e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0216744, Final residual = 1.57713e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00227412, Final residual = 2.12966e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00158243, Final residual = 1.64477e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00156029, Final residual = 1.75448e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00156059, Final residual = 1.7576e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00280916, Final residual = 1.89152e-07, No Iterations 1 +min/max(T) = 724.672, 2809.02 +GAMG: Solving for p, Initial residual = 0.0346707, Final residual = 0.00114183, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.68516e-05, global = 1.05095e-05, cumulative = 0.00276264 +GAMG: Solving for p, Initial residual = 0.00108777, Final residual = 3.72695e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.11472e-05, global = 1.11457e-05, cumulative = 0.00277379 +smoothSolver: Solving for epsilon, Initial residual = 0.000832092, Final residual = 1.61248e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00136152, Final residual = 3.93374e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100537 s +other Time = 1e-06 s +rho Equations = 0.00018 s +U Equations = 0.001224 s +Y Equations = 0.00252882 s +E Equations = 0.000595 s +p Equations = 0.002628 s +calculate parcels = 100.08 s +chemistry correctThermo = 0.002862 s +turbulence correct = 0.001096 s +combustion correct(in Y) = 0.0892242 s +percentage of chemistry = 88.7476 % +percentage of rho/U/Y/E = 4.50364 % +========Time details of each equation======= +rhoEqn Time = 0.000334 s +rhoEqn assamble = 0.00025 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001224 s +UEqn assamble = 0.000713 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000511 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001881 s +YEqn assamble = 0.000682 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000205 s +YEqn correct boundary = 0 s +EEqn Time = 0.000439 s +EEqn assamble = 0.000324 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 151.51 s ClockTime = 152 s +Courant Number mean: 0.00809624 max: 0.0332382 +Time = 0.0013725 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22482 + Current mass in system = 1.5839e-09 + Linear momentum = (1.824e-11 -1.12272e-08 0) + |Linear momentum| = 1.12272e-08 + Linear kinetic energy = 4.12484e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 386.501, 540.2 + Mass transfer phase change = 1.2224e-10 + D10, D32, Dmax (mu) = 62.6324, 88.9048, 157.572 + Liquid penetration 95% mass (m) = 0.00992334 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0262246, Final residual = 2.12003e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0223668, Final residual = 1.62472e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00202667, Final residual = 1.69137e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00157373, Final residual = 1.59974e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00156702, Final residual = 1.75618e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00156726, Final residual = 1.7596e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00270345, Final residual = 1.72215e-07, No Iterations 1 +min/max(T) = 724.203, 2810.57 +GAMG: Solving for p, Initial residual = 0.0319273, Final residual = 0.000929052, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.55288e-05, global = 9.40342e-06, cumulative = 0.00278319 +GAMG: Solving for p, Initial residual = 0.000883003, Final residual = 6.45127e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.03223e-05, global = 1.03192e-05, cumulative = 0.00279351 +smoothSolver: Solving for epsilon, Initial residual = 0.000843964, Final residual = 1.63953e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00136904, Final residual = 3.93607e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.078057 s +other Time = 0 s +rho Equations = 0.000188 s +U Equations = 0.001105 s +Y Equations = 0.00235689 s +E Equations = 0.000506 s +p Equations = 0.002059 s +calculate parcels = 100.357 s +chemistry correctThermo = 0.001953 s +turbulence correct = 0.000862 s +combustion correct(in Y) = 0.0688371 s +percentage of chemistry = 88.1883 % +percentage of rho/U/Y/E = 5.32417 % +========Time details of each equation======= +rhoEqn Time = 0.000311 s +rhoEqn assamble = 0.000237 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001103 s +UEqn assamble = 0.000667 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000436 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001776 s +YEqn assamble = 0.000595 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000155 s +YEqn correct boundary = 0 s +EEqn Time = 0.000379 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 151.86 s ClockTime = 152 s +Courant Number mean: 0.00795237 max: 0.0337917 +Time = 0.001375 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22480 + Current mass in system = 1.58299e-09 + Linear momentum = (1.79064e-11 -1.11954e-08 0) + |Linear momentum| = 1.11954e-08 + Linear kinetic energy = 4.1045e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 386.63, 540.2 + Mass transfer phase change = 1.23149e-10 + D10, D32, Dmax (mu) = 62.7295, 88.8996, 157.687 + Liquid penetration 95% mass (m) = 0.00994234 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0252921, Final residual = 2.0486e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0234691, Final residual = 1.66392e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00210618, Final residual = 1.73638e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0015733, Final residual = 1.601e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00156134, Final residual = 1.75355e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0015616, Final residual = 1.75695e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00268388, Final residual = 1.72578e-07, No Iterations 1 +min/max(T) = 723.909, 2811.07 +GAMG: Solving for p, Initial residual = 0.0296199, Final residual = 0.000783944, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.43679e-05, global = 9.98354e-06, cumulative = 0.00280349 +GAMG: Solving for p, Initial residual = 0.000728221, Final residual = 5.728e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.04705e-05, global = 1.04683e-05, cumulative = 0.00281396 +smoothSolver: Solving for epsilon, Initial residual = 0.000879531, Final residual = 1.70879e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00140281, Final residual = 4.02436e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.113376 s +other Time = 0 s +rho Equations = 0.000241 s +U Equations = 0.001668 s +Y Equations = 0.00265925 s +E Equations = 0.000602 s +p Equations = 0.002381 s +calculate parcels = 100.699 s +chemistry correctThermo = 0.002804 s +turbulence correct = 0.000948 s +combustion correct(in Y) = 0.101839 s +percentage of chemistry = 89.8239 % +percentage of rho/U/Y/E = 4.56027 % +========Time details of each equation======= +rhoEqn Time = 0.0004 s +rhoEqn assamble = 0.000309 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001666 s +UEqn assamble = 0.000916 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00075 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001607 s +YEqn assamble = 0.000641 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -2.3e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000445 s +EEqn assamble = 0.000331 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 152.32 s ClockTime = 153 s +Courant Number mean: 0.00780954 max: 0.0337632 +Time = 0.0013775 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22472 + Current mass in system = 1.58175e-09 + Linear momentum = (1.77856e-11 -1.11618e-08 0) + |Linear momentum| = 1.11618e-08 + Linear kinetic energy = 4.08369e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 386.763, 540.2 + Mass transfer phase change = 1.24395e-10 + D10, D32, Dmax (mu) = 62.9403, 88.9421, 157.807 + Liquid penetration 95% mass (m) = 0.00996041 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0194482, Final residual = 1.47897e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0242234, Final residual = 1.64659e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00299642, Final residual = 3.06659e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00158055, Final residual = 1.5936e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00155215, Final residual = 1.76648e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00155248, Final residual = 1.76991e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0027933, Final residual = 1.86384e-07, No Iterations 1 +min/max(T) = 723.771, 2811.89 +GAMG: Solving for p, Initial residual = 0.0292736, Final residual = 0.00126315, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.87398e-05, global = 1.22342e-05, cumulative = 0.0028262 +GAMG: Solving for p, Initial residual = 0.00119003, Final residual = 8.45641e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.43657e-05, global = 1.43629e-05, cumulative = 0.00284056 +smoothSolver: Solving for epsilon, Initial residual = 0.00096864, Final residual = 1.84566e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00146452, Final residual = 4.16873e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.101834 s +other Time = 0 s +rho Equations = 0.00018 s +U Equations = 0.001224 s +Y Equations = 0.00230806 s +E Equations = 0.000484 s +p Equations = 0.00196 s +calculate parcels = 101.059 s +chemistry correctThermo = 0.002021 s +turbulence correct = 0.000807 s +combustion correct(in Y) = 0.0926149 s +percentage of chemistry = 90.947 % +percentage of rho/U/Y/E = 4.12049 % +========Time details of each equation======= +rhoEqn Time = 0.000296 s +rhoEqn assamble = 0.000235 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001223 s +UEqn assamble = 0.0007 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000523 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001628 s +YEqn assamble = 0.000672 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.6e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000367 s +EEqn assamble = 0.000273 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 152.78 s ClockTime = 153 s +Courant Number mean: 0.00764685 max: 0.0344222 +Time = 0.00138 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22463 + Current mass in system = 1.58044e-09 + Linear momentum = (1.80762e-11 -1.11253e-08 0) + |Linear momentum| = 1.11253e-08 + Linear kinetic energy = 4.0612e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 386.896, 540.2 + Mass transfer phase change = 1.25703e-10 + D10, D32, Dmax (mu) = 63.1309, 88.9741, 157.925 + Liquid penetration 95% mass (m) = 0.00997981 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0248947, Final residual = 1.74537e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0258276, Final residual = 1.68638e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00304451, Final residual = 3.30515e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00152082, Final residual = 1.58253e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00146295, Final residual = 1.67522e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00146331, Final residual = 1.67853e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00276842, Final residual = 1.92576e-07, No Iterations 1 +min/max(T) = 723.572, 2813.24 +GAMG: Solving for p, Initial residual = 0.0304091, Final residual = 0.00119402, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.98488e-05, global = 1.36077e-05, cumulative = 0.00285417 +GAMG: Solving for p, Initial residual = 0.00113162, Final residual = 5.40173e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.50852e-05, global = 1.50824e-05, cumulative = 0.00286925 +smoothSolver: Solving for epsilon, Initial residual = 0.00093432, Final residual = 1.75139e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00144565, Final residual = 4.06422e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.101933 s +other Time = 0 s +rho Equations = 0.000155 s +U Equations = 0.000991 s +Y Equations = 0.00272187 s +E Equations = 0.00095 s +p Equations = 0.001935 s +calculate parcels = 101.405 s +chemistry correctThermo = 0.004875 s +turbulence correct = 0.000822 s +combustion correct(in Y) = 0.0892611 s +percentage of chemistry = 87.5684 % +percentage of rho/U/Y/E = 4.72651 % +========Time details of each equation======= +rhoEqn Time = 0.000268 s +rhoEqn assamble = 0.00021 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000989 s +UEqn assamble = 0.000559 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00043 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002171 s +YEqn assamble = 0.00068 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000492 s +YEqn correct boundary = 0 s +EEqn Time = 0.000699 s +EEqn assamble = 0.000507 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000192 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 153.23 s ClockTime = 154 s +Courant Number mean: 0.00746297 max: 0.0346465 +Time = 0.0013825 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22456 + Current mass in system = 1.57924e-09 + Linear momentum = (1.9089e-11 -1.10865e-08 0) + |Linear momentum| = 1.10865e-08 + Linear kinetic energy = 4.03694e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 387.027, 540.2 + Mass transfer phase change = 1.26901e-10 + D10, D32, Dmax (mu) = 63.314, 88.967, 158.046 + Liquid penetration 95% mass (m) = 0.0099994 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0290803, Final residual = 1.81726e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0275612, Final residual = 1.76603e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00264852, Final residual = 2.61368e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00146015, Final residual = 1.55525e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00145194, Final residual = 1.71962e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00145226, Final residual = 1.72297e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00260004, Final residual = 1.8464e-07, No Iterations 1 +min/max(T) = 723.164, 2815.22 +GAMG: Solving for p, Initial residual = 0.0279315, Final residual = 0.00115173, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.06952e-05, global = 1.23562e-05, cumulative = 0.00288161 +GAMG: Solving for p, Initial residual = 0.00109221, Final residual = 2.11939e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.38096e-05, global = 1.38081e-05, cumulative = 0.00289541 +smoothSolver: Solving for epsilon, Initial residual = 0.000926231, Final residual = 1.73318e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00143476, Final residual = 4.0043e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.112887 s +other Time = 1e-06 s +rho Equations = 0.00018 s +U Equations = 0.001192 s +Y Equations = 0.00211837 s +E Equations = 0.000483 s +p Equations = 0.002003 s +calculate parcels = 101.758 s +chemistry correctThermo = 0.002038 s +turbulence correct = 0.000942 s +combustion correct(in Y) = 0.103726 s +percentage of chemistry = 91.8845 % +percentage of rho/U/Y/E = 3.51978 % +========Time details of each equation======= +rhoEqn Time = 0.000295 s +rhoEqn assamble = 0.000233 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001191 s +UEqn assamble = 0.000668 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000523 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001459 s +YEqn assamble = 0.000524 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000109 s +YEqn correct boundary = 0 s +EEqn Time = 0.000364 s +EEqn assamble = 0.000271 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 153.7 s ClockTime = 154 s +Courant Number mean: 0.00728942 max: 0.0355226 +Time = 0.001385 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22448 + Current mass in system = 1.57816e-09 + Linear momentum = (1.95262e-11 -1.10467e-08 0) + |Linear momentum| = 1.10467e-08 + Linear kinetic energy = 4.01182e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 387.155, 540.2 + Mass transfer phase change = 1.27988e-10 + D10, D32, Dmax (mu) = 63.9443, 88.9432, 158.177 + Liquid penetration 95% mass (m) = 0.0100183 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0290236, Final residual = 1.94479e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0287807, Final residual = 1.83697e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00232058, Final residual = 2.17187e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00143691, Final residual = 1.50418e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00143339, Final residual = 1.65676e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00143367, Final residual = 1.66035e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00250066, Final residual = 1.71072e-07, No Iterations 1 +min/max(T) = 722.799, 2816.6 +GAMG: Solving for p, Initial residual = 0.0261603, Final residual = 0.0010979, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.98707e-05, global = 1.09753e-05, cumulative = 0.00290639 +GAMG: Solving for p, Initial residual = 0.00104483, Final residual = 6.94997e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.25247e-05, global = 1.25205e-05, cumulative = 0.00291891 +smoothSolver: Solving for epsilon, Initial residual = 0.000905563, Final residual = 1.70294e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00142446, Final residual = 3.94115e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.076569 s +other Time = 1e-06 s +rho Equations = 0.000165 s +U Equations = 0.001199 s +Y Equations = 0.00262495 s +E Equations = 0.000534 s +p Equations = 0.002004 s +calculate parcels = 102.097 s +chemistry correctThermo = 0.001927 s +turbulence correct = 0.000834 s +combustion correct(in Y) = 0.067087 s +percentage of chemistry = 87.6165 % +percentage of rho/U/Y/E = 5.90703 % +========Time details of each equation======= +rhoEqn Time = 0.000287 s +rhoEqn assamble = 0.000226 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001198 s +UEqn assamble = 0.000703 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000495 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002048 s +YEqn assamble = 0.000648 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000259 s +YEqn correct boundary = 0 s +EEqn Time = 0.000386 s +EEqn assamble = 0.00029 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 154.11 s ClockTime = 155 s +Courant Number mean: 0.00712281 max: 0.0364796 +Time = 0.0013875 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22446 + Current mass in system = 1.57714e-09 + Linear momentum = (1.96258e-11 -1.10078e-08 0) + |Linear momentum| = 1.10078e-08 + Linear kinetic energy = 3.98717e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 387.282, 540.2 + Mass transfer phase change = 1.29004e-10 + D10, D32, Dmax (mu) = 63.9361, 88.9024, 158.313 + Liquid penetration 95% mass (m) = 0.0100366 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0279429, Final residual = 1.99919e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0301743, Final residual = 1.89162e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00223158, Final residual = 1.86689e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00143758, Final residual = 1.4739e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00143133, Final residual = 1.63779e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00143152, Final residual = 1.64131e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00246699, Final residual = 1.62818e-07, No Iterations 1 +min/max(T) = 722.68, 2817.06 +GAMG: Solving for p, Initial residual = 0.0248008, Final residual = 0.00092125, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.74502e-05, global = 1.11879e-05, cumulative = 0.0029301 +GAMG: Solving for p, Initial residual = 0.000864751, Final residual = 5.29552e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.1713e-05, global = 1.17103e-05, cumulative = 0.00294181 +smoothSolver: Solving for epsilon, Initial residual = 0.00094154, Final residual = 1.77243e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00144966, Final residual = 3.98799e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.120694 s +other Time = 0 s +rho Equations = 0.000191 s +U Equations = 0.001278 s +Y Equations = 0.00208006 s +E Equations = 0.000472 s +p Equations = 0.002383 s +calculate parcels = 102.411 s +chemistry correctThermo = 0.002471 s +turbulence correct = 0.000989 s +combustion correct(in Y) = 0.110622 s +percentage of chemistry = 91.6549 % +percentage of rho/U/Y/E = 3.33161 % +========Time details of each equation======= +rhoEqn Time = 0.000363 s +rhoEqn assamble = 0.000289 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001277 s +UEqn assamble = 0.000758 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000519 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001405 s +YEqn assamble = 0.00052 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 6.7e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000356 s +EEqn assamble = 0.000266 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 154.55 s ClockTime = 155 s +Courant Number mean: 0.00696688 max: 0.037433 +Time = 0.00139 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22441 + Current mass in system = 1.57595e-09 + Linear momentum = (1.94632e-11 -1.09686e-08 0) + |Linear momentum| = 1.09686e-08 + Linear kinetic energy = 3.96275e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 387.417, 540.2 + Mass transfer phase change = 1.30188e-10 + D10, D32, Dmax (mu) = 63.8687, 88.8897, 158.44 + Liquid penetration 95% mass (m) = 0.0100565 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.024813, Final residual = 1.71228e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0311219, Final residual = 1.87562e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0026811, Final residual = 2.48635e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00144098, Final residual = 1.46792e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00140018, Final residual = 1.6107e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00140043, Final residual = 1.61428e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00250306, Final residual = 1.7223e-07, No Iterations 1 +min/max(T) = 722.749, 2817.1 +GAMG: Solving for p, Initial residual = 0.0235028, Final residual = 0.00114257, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.87851e-05, global = 1.13704e-05, cumulative = 0.00295318 +GAMG: Solving for p, Initial residual = 0.00107997, Final residual = 6.96135e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.36537e-05, global = 1.36515e-05, cumulative = 0.00296683 +smoothSolver: Solving for epsilon, Initial residual = 0.00101125, Final residual = 1.89509e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00150667, Final residual = 4.12666e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.104236 s +other Time = 1e-06 s +rho Equations = 0.000182 s +U Equations = 0.00122 s +Y Equations = 0.00246696 s +E Equations = 0.000598 s +p Equations = 0.002579 s +calculate parcels = 102.808 s +chemistry correctThermo = 0.002865 s +turbulence correct = 0.001157 s +combustion correct(in Y) = 0.092964 s +percentage of chemistry = 89.1861 % +percentage of rho/U/Y/E = 4.28543 % +========Time details of each equation======= +rhoEqn Time = 0.000334 s +rhoEqn assamble = 0.000262 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001218 s +UEqn assamble = 0.000709 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000509 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001804 s +YEqn assamble = 0.000629 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00018 s +YEqn correct boundary = 0 s +EEqn Time = 0.000442 s +EEqn assamble = 0.000327 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 155.05 s ClockTime = 156 s +Courant Number mean: 0.00679946 max: 0.0382477 +Time = 0.0013925 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22433 + Current mass in system = 1.5747e-09 + Linear momentum = (1.95887e-11 -1.09279e-08 0) + |Linear momentum| = 1.09279e-08 + Linear kinetic energy = 3.93761e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 387.556, 540.2 + Mass transfer phase change = 1.31443e-10 + D10, D32, Dmax (mu) = 64.1009, 88.8798, 158.549 + Liquid penetration 95% mass (m) = 0.0100746 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0241926, Final residual = 1.48063e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.03257, Final residual = 1.87148e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00275698, Final residual = 2.63301e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00142081, Final residual = 1.43286e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00138907, Final residual = 1.57952e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00138927, Final residual = 1.58316e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00247674, Final residual = 1.72213e-07, No Iterations 1 +min/max(T) = 722.794, 2817.7 +GAMG: Solving for p, Initial residual = 0.0230548, Final residual = 0.000874112, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.88146e-05, global = 1.37509e-05, cumulative = 0.00298058 +GAMG: Solving for p, Initial residual = 0.000814636, Final residual = 5.07629e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.44615e-05, global = 1.44582e-05, cumulative = 0.00299504 +smoothSolver: Solving for epsilon, Initial residual = 0.00106464, Final residual = 2.0047e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00155461, Final residual = 4.27284e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.105804 s +other Time = 0 s +rho Equations = 0.000157 s +U Equations = 0.001004 s +Y Equations = 0.0025768 s +E Equations = 0.000628 s +p Equations = 0.002719 s +calculate parcels = 103.176 s +chemistry correctThermo = 0.002874 s +turbulence correct = 0.001163 s +combustion correct(in Y) = 0.0944862 s +percentage of chemistry = 89.3031 % +percentage of rho/U/Y/E = 4.12631 % +========Time details of each equation======= +rhoEqn Time = 0.000314 s +rhoEqn assamble = 0.000252 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001004 s +UEqn assamble = 0.000585 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000419 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002033 s +YEqn assamble = 0.000713 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000265 s +YEqn correct boundary = 0 s +EEqn Time = 0.000452 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 155.52 s ClockTime = 156 s +Courant Number mean: 0.00662021 max: 0.0388676 +Time = 0.001395 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22428 + Current mass in system = 1.5735e-09 + Linear momentum = (1.9389e-11 -1.08862e-08 0) + |Linear momentum| = 1.08862e-08 + Linear kinetic energy = 3.91162e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 387.686, 540.2 + Mass transfer phase change = 1.32645e-10 + D10, D32, Dmax (mu) = 64.2249, 88.8453, 158.656 + Liquid penetration 95% mass (m) = 0.0100931 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0247789, Final residual = 1.59708e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0340642, Final residual = 1.9193e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00249159, Final residual = 2.22132e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00138498, Final residual = 1.37554e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00138023, Final residual = 1.52919e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00138044, Final residual = 1.53263e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00239364, Final residual = 1.53647e-07, No Iterations 1 +min/max(T) = 722.711, 2818.3 +GAMG: Solving for p, Initial residual = 0.021995, Final residual = 0.00120559, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.17065e-05, global = 1.06863e-05, cumulative = 0.00300573 +GAMG: Solving for p, Initial residual = 0.00115202, Final residual = 7.61912e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.38622e-05, global = 1.38565e-05, cumulative = 0.00301958 +smoothSolver: Solving for epsilon, Initial residual = 0.00100055, Final residual = 1.86981e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00151228, Final residual = 4.14409e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092792 s +other Time = 1e-06 s +rho Equations = 0.000183 s +U Equations = 0.00123 s +Y Equations = 0.00219925 s +E Equations = 0.000513 s +p Equations = 0.002075 s +calculate parcels = 103.541 s +chemistry correctThermo = 0.00211 s +turbulence correct = 0.000839 s +combustion correct(in Y) = 0.0834448 s +percentage of chemistry = 89.9267 % +percentage of rho/U/Y/E = 4.44569 % +========Time details of each equation======= +rhoEqn Time = 0.000303 s +rhoEqn assamble = 0.000238 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001228 s +UEqn assamble = 0.000668 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00056 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001556 s +YEqn assamble = 0.000557 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000118 s +YEqn correct boundary = 0 s +EEqn Time = 0.000387 s +EEqn assamble = 0.000287 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.0001 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 155.98 s ClockTime = 156 s +Courant Number mean: 0.00642 max: 0.0392205 +Time = 0.0013975 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22428 + Current mass in system = 1.57247e-09 + Linear momentum = (1.84763e-11 -1.0844e-08 0) + |Linear momentum| = 1.0844e-08 + Linear kinetic energy = 3.88523e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 387.816, 540.2 + Mass transfer phase change = 1.33673e-10 + D10, D32, Dmax (mu) = 64.0327, 88.7839, 158.771 + Liquid penetration 95% mass (m) = 0.0101126 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0255018, Final residual = 1.54172e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0356418, Final residual = 1.99247e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00210661, Final residual = 1.59804e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00134557, Final residual = 1.37754e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00134803, Final residual = 1.51718e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00134828, Final residual = 1.52063e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00228958, Final residual = 1.48599e-07, No Iterations 1 +min/max(T) = 722.624, 2819.12 +GAMG: Solving for p, Initial residual = 0.0203368, Final residual = 0.000853584, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.79473e-05, global = 1.03969e-05, cumulative = 0.00302998 +GAMG: Solving for p, Initial residual = 0.000806496, Final residual = 5.9455e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.18528e-05, global = 1.18492e-05, cumulative = 0.00304183 +smoothSolver: Solving for epsilon, Initial residual = 0.000988414, Final residual = 1.86056e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00150844, Final residual = 4.09389e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.099764 s +other Time = 1e-06 s +rho Equations = 0.000182 s +U Equations = 0.001182 s +Y Equations = 0.00235001 s +E Equations = 0.000499 s +p Equations = 0.002004 s +calculate parcels = 103.879 s +chemistry correctThermo = 0.002004 s +turbulence correct = 0.000856 s +combustion correct(in Y) = 0.090494 s +percentage of chemistry = 90.7081 % +percentage of rho/U/Y/E = 4.22298 % +========Time details of each equation======= +rhoEqn Time = 0.000308 s +rhoEqn assamble = 0.000241 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001181 s +UEqn assamble = 0.00066 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000521 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001702 s +YEqn assamble = 0.000682 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.7e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.00037 s +EEqn assamble = 0.000278 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 156.42 s ClockTime = 157 s +Courant Number mean: 0.0062443 max: 0.0397091 +Time = 0.0014 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22426 + Current mass in system = 1.57134e-09 + Linear momentum = (1.77027e-11 -1.08024e-08 0) + |Linear momentum| = 1.08024e-08 + Linear kinetic energy = 3.85945e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 387.946, 540.2 + Mass transfer phase change = 1.34804e-10 + D10, D32, Dmax (mu) = 63.9423, 88.7529, 158.988 + Liquid penetration 95% mass (m) = 0.0101307 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0235044, Final residual = 1.45606e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0371369, Final residual = 2.03806e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0023624, Final residual = 1.93028e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00135173, Final residual = 1.38639e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0013324, Final residual = 1.52676e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00133265, Final residual = 1.5302e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00229421, Final residual = 1.53837e-07, No Iterations 1 +min/max(T) = 722.786, 2819.43 +GAMG: Solving for p, Initial residual = 0.0196796, Final residual = 0.00063188, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.67859e-05, global = 1.22723e-05, cumulative = 0.0030541 +GAMG: Solving for p, Initial residual = 0.000592428, Final residual = 4.42354e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.30383e-05, global = 1.30363e-05, cumulative = 0.00306714 +smoothSolver: Solving for epsilon, Initial residual = 0.0010034, Final residual = 1.88208e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00151105, Final residual = 4.06244e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.087586 s +other Time = 1e-06 s +rho Equations = 0.000177 s +U Equations = 0.001081 s +Y Equations = 0.00250097 s +E Equations = 0.000619 s +p Equations = 0.00236 s +calculate parcels = 104.143 s +chemistry correctThermo = 0.002829 s +turbulence correct = 0.000965 s +combustion correct(in Y) = 0.076877 s +percentage of chemistry = 87.7732 % +percentage of rho/U/Y/E = 4.99848 % +========Time details of each equation======= +rhoEqn Time = 0.000321 s +rhoEqn assamble = 0.000253 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001079 s +UEqn assamble = 0.000617 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000462 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001898 s +YEqn assamble = 0.000643 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000295 s +YEqn correct boundary = 0 s +EEqn Time = 0.000454 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 157.13 s ClockTime = 158 s +Courant Number mean: 0.00607838 max: 0.0408703 +Time = 0.0014025 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22426 + Current mass in system = 1.5703e-09 + Linear momentum = (1.72811e-11 -1.07623e-08 0) + |Linear momentum| = 1.07623e-08 + Linear kinetic energy = 3.83457e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 388.077, 540.2 + Mass transfer phase change = 1.35838e-10 + D10, D32, Dmax (mu) = 63.7926, 88.7094, 159.202 + Liquid penetration 95% mass (m) = 0.0101484 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0184631, Final residual = 1.26814e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0378732, Final residual = 2.01337e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00214137, Final residual = 1.66219e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00133596, Final residual = 1.39381e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00132986, Final residual = 1.53508e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0013301, Final residual = 1.53843e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00224358, Final residual = 1.53266e-07, No Iterations 1 +min/max(T) = 723.16, 2819.39 +GAMG: Solving for p, Initial residual = 0.0184892, Final residual = 0.000524385, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.49374e-05, global = 1.13054e-05, cumulative = 0.00307844 +GAMG: Solving for p, Initial residual = 0.000495448, Final residual = 3.66874e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.19238e-05, global = 1.19222e-05, cumulative = 0.00309036 +smoothSolver: Solving for epsilon, Initial residual = 0.000998771, Final residual = 1.8997e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00150885, Final residual = 4.06099e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.111706 s +other Time = 1e-06 s +rho Equations = 0.000168 s +U Equations = 0.001206 s +Y Equations = 0.0025323 s +E Equations = 0.000597 s +p Equations = 0.002463 s +calculate parcels = 104.504 s +chemistry correctThermo = 0.002849 s +turbulence correct = 0.001114 s +combustion correct(in Y) = 0.100569 s +percentage of chemistry = 90.0298 % +percentage of rho/U/Y/E = 4.03139 % +========Time details of each equation======= +rhoEqn Time = 0.000307 s +rhoEqn assamble = 0.000243 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001203 s +UEqn assamble = 0.000703 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.0005 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001886 s +YEqn assamble = 0.000682 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000205 s +YEqn correct boundary = 0 s +EEqn Time = 0.000434 s +EEqn assamble = 0.000323 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 157.6 s ClockTime = 158 s +Courant Number mean: 0.00591261 max: 0.0421211 +Time = 0.001405 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22425 + Current mass in system = 1.56922e-09 + Linear momentum = (1.70601e-11 -1.07232e-08 0) + |Linear momentum| = 1.07232e-08 + Linear kinetic energy = 3.81048e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 388.209, 540.2 + Mass transfer phase change = 1.36922e-10 + D10, D32, Dmax (mu) = 63.6832, 88.68, 159.417 + Liquid penetration 95% mass (m) = 0.0101661 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.016949, Final residual = 1.12072e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0391942, Final residual = 1.98325e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0022661, Final residual = 1.86185e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00133662, Final residual = 1.38019e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00132271, Final residual = 1.49992e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00132296, Final residual = 1.50314e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00222436, Final residual = 1.5314e-07, No Iterations 1 +min/max(T) = 723.62, 2819.38 +GAMG: Solving for p, Initial residual = 0.0175555, Final residual = 0.000414251, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.48892e-05, global = 1.19037e-05, cumulative = 0.00310227 +GAMG: Solving for p, Initial residual = 0.000391037, Final residual = 2.46573e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.24979e-05, global = 1.24964e-05, cumulative = 0.00311476 +smoothSolver: Solving for epsilon, Initial residual = 0.0010026, Final residual = 1.92802e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0015118, Final residual = 4.08684e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.105161 s +other Time = 0 s +rho Equations = 0.000174 s +U Equations = 0.001217 s +Y Equations = 0.00217452 s +E Equations = 0.000491 s +p Equations = 0.002126 s +calculate parcels = 104.873 s +chemistry correctThermo = 0.002027 s +turbulence correct = 0.001 s +combustion correct(in Y) = 0.0957595 s +percentage of chemistry = 91.0599 % +percentage of rho/U/Y/E = 3.85744 % +========Time details of each equation======= +rhoEqn Time = 0.000316 s +rhoEqn assamble = 0.00024 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001216 s +UEqn assamble = 0.000693 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000523 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001516 s +YEqn assamble = 0.000538 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000115 s +YEqn correct boundary = 0 s +EEqn Time = 0.000371 s +EEqn assamble = 0.000278 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 158.08 s ClockTime = 159 s +Courant Number mean: 0.00573745 max: 0.0428466 +Time = 0.0014075 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22424 + Current mass in system = 1.56817e-09 + Linear momentum = (1.69957e-11 -1.06847e-08 0) + |Linear momentum| = 1.06847e-08 + Linear kinetic energy = 3.78684e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 388.343, 540.2 + Mass transfer phase change = 1.37977e-10 + D10, D32, Dmax (mu) = 63.6571, 88.6444, 159.638 + Liquid penetration 95% mass (m) = 0.0101856 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0147158, Final residual = 1.02214e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0405534, Final residual = 1.94636e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00214913, Final residual = 1.65595e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00132208, Final residual = 1.34795e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00131713, Final residual = 1.48484e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00131738, Final residual = 1.48813e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00219417, Final residual = 1.45814e-07, No Iterations 1 +min/max(T) = 724.09, 2819.48 +GAMG: Solving for p, Initial residual = 0.0172248, Final residual = 0.000424285, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.48219e-05, global = 1.14559e-05, cumulative = 0.00312622 +GAMG: Solving for p, Initial residual = 0.000400202, Final residual = 2.59798e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.21586e-05, global = 1.21567e-05, cumulative = 0.00313838 +smoothSolver: Solving for epsilon, Initial residual = 0.00099749, Final residual = 1.91963e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00150937, Final residual = 4.07354e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.106175 s +other Time = 0 s +rho Equations = 0.000182 s +U Equations = 0.001207 s +Y Equations = 0.00255697 s +E Equations = 0.000689 s +p Equations = 0.002437 s +calculate parcels = 105.223 s +chemistry correctThermo = 0.002895 s +turbulence correct = 0.000982 s +combustion correct(in Y) = 0.095031 s +percentage of chemistry = 89.5041 % +percentage of rho/U/Y/E = 4.36541 % +========Time details of each equation======= +rhoEqn Time = 0.000336 s +rhoEqn assamble = 0.000265 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001207 s +UEqn assamble = 0.000679 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000528 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001899 s +YEqn assamble = 0.00069 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000216 s +YEqn correct boundary = 0 s +EEqn Time = 0.000511 s +EEqn assamble = 0.000386 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000125 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 158.53 s ClockTime = 159 s +Courant Number mean: 0.00555939 max: 0.0431782 +Time = 0.00141 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22423 + Current mass in system = 1.5671e-09 + Linear momentum = (1.70262e-11 -1.06466e-08 0) + |Linear momentum| = 1.06466e-08 + Linear kinetic energy = 3.76351e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 388.467, 540.2 + Mass transfer phase change = 1.39046e-10 + D10, D32, Dmax (mu) = 63.6218, 88.6127, 159.858 + Liquid penetration 95% mass (m) = 0.0102038 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0110919, Final residual = 8.56594e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0419559, Final residual = 1.94414e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00216647, Final residual = 1.67005e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00130506, Final residual = 1.338e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0012988, Final residual = 1.47746e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00129906, Final residual = 1.48074e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00217132, Final residual = 1.4405e-07, No Iterations 1 +min/max(T) = 724.593, 2819.49 +GAMG: Solving for p, Initial residual = 0.0166433, Final residual = 0.000291603, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.44055e-05, global = 1.19316e-05, cumulative = 0.00315031 +GAMG: Solving for p, Initial residual = 0.000275909, Final residual = 7.61644e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.23216e-05, global = 1.23154e-05, cumulative = 0.00316262 +smoothSolver: Solving for epsilon, Initial residual = 0.000997993, Final residual = 1.91137e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00150721, Final residual = 4.03504e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.079829 s +other Time = 1e-06 s +rho Equations = 0.000172 s +U Equations = 0.001061 s +Y Equations = 0.00224739 s +E Equations = 0.000501 s +p Equations = 0.001902 s +calculate parcels = 105.557 s +chemistry correctThermo = 0.002095 s +turbulence correct = 0.000869 s +combustion correct(in Y) = 0.0707876 s +percentage of chemistry = 88.6741 % +percentage of rho/U/Y/E = 4.9874 % +========Time details of each equation======= +rhoEqn Time = 0.0003 s +rhoEqn assamble = 0.000239 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00106 s +UEqn assamble = 0.00064 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00042 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001665 s +YEqn assamble = 0.000544 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000134 s +YEqn correct boundary = 0 s +EEqn Time = 0.00038 s +EEqn assamble = 0.000287 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 158.95 s ClockTime = 159 s +Courant Number mean: 0.00537632 max: 0.0433719 +Time = 0.0014125 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22420 + Current mass in system = 1.56593e-09 + Linear momentum = (1.69911e-11 -1.06086e-08 0) + |Linear momentum| = 1.06086e-08 + Linear kinetic energy = 3.74046e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 388.584, 540.2 + Mass transfer phase change = 1.4021e-10 + D10, D32, Dmax (mu) = 63.7441, 88.5953, 160.079 + Liquid penetration 95% mass (m) = 0.0102228 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0097191, Final residual = 7.11131e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0438096, Final residual = 1.98498e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0023654, Final residual = 1.82827e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00128807, Final residual = 1.31511e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00128635, Final residual = 1.45633e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00128661, Final residual = 1.45957e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00218529, Final residual = 1.42677e-07, No Iterations 1 +min/max(T) = 725.182, 2819.37 +GAMG: Solving for p, Initial residual = 0.0163904, Final residual = 0.000382262, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.54475e-05, global = 1.25941e-05, cumulative = 0.00317522 +GAMG: Solving for p, Initial residual = 0.000365696, Final residual = 3.41298e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.34166e-05, global = 1.3415e-05, cumulative = 0.00318863 +smoothSolver: Solving for epsilon, Initial residual = 0.00100642, Final residual = 1.92529e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00150348, Final residual = 3.98239e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097287 s +other Time = 0 s +rho Equations = 0.000187 s +U Equations = 0.001199 s +Y Equations = 0.00209105 s +E Equations = 0.00048 s +p Equations = 0.001937 s +calculate parcels = 105.846 s +chemistry correctThermo = 0.002002 s +turbulence correct = 0.00081 s +combustion correct(in Y) = 0.088331 s +percentage of chemistry = 90.7942 % +percentage of rho/U/Y/E = 4.0674 % +========Time details of each equation======= +rhoEqn Time = 0.000303 s +rhoEqn assamble = 0.000237 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001196 s +UEqn assamble = 0.000706 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00049 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001451 s +YEqn assamble = 0.000506 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000362 s +EEqn assamble = 0.00027 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 159.33 s ClockTime = 160 s +Courant Number mean: 0.00518424 max: 0.0435066 +Time = 0.001415 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22415 + Current mass in system = 1.56463e-09 + Linear momentum = (1.73273e-11 -1.05702e-08 0) + |Linear momentum| = 1.05702e-08 + Linear kinetic energy = 3.71753e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 388.699, 540.2 + Mass transfer phase change = 1.41512e-10 + D10, D32, Dmax (mu) = 63.9119, 88.5939, 160.307 + Liquid penetration 95% mass (m) = 0.0102406 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0159825, Final residual = 1.14196e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.046341, Final residual = 2.06524e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00265869, Final residual = 2.37047e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00125314, Final residual = 1.29298e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00124919, Final residual = 1.43823e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00124945, Final residual = 1.4415e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00220929, Final residual = 1.52642e-07, No Iterations 1 +min/max(T) = 725.865, 2819.44 +GAMG: Solving for p, Initial residual = 0.0167167, Final residual = 0.000545648, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.74134e-05, global = 1.35857e-05, cumulative = 0.00320222 +GAMG: Solving for p, Initial residual = 0.000526596, Final residual = 9.9217e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.5014e-05, global = 1.50087e-05, cumulative = 0.00321723 +smoothSolver: Solving for epsilon, Initial residual = 0.00104411, Final residual = 1.9515e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0015232, Final residual = 3.96643e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.098965 s +other Time = 1e-06 s +rho Equations = 0.000145 s +U Equations = 0.001048 s +Y Equations = 0.00224712 s +E Equations = 0.000496 s +p Equations = 0.001862 s +calculate parcels = 106.209 s +chemistry correctThermo = 0.002026 s +turbulence correct = 0.000863 s +combustion correct(in Y) = 0.0901059 s +percentage of chemistry = 91.0482 % +percentage of rho/U/Y/E = 3.97728 % +========Time details of each equation======= +rhoEqn Time = 0.000278 s +rhoEqn assamble = 0.000213 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001046 s +UEqn assamble = 0.000635 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000411 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001701 s +YEqn assamble = 0.000568 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000158 s +YEqn correct boundary = 0 s +EEqn Time = 0.000374 s +EEqn assamble = 0.000282 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 159.79 s ClockTime = 160 s +Courant Number mean: 0.004976 max: 0.0431759 +Time = 0.0014175 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22413 + Current mass in system = 1.5635e-09 + Linear momentum = (1.86988e-11 -1.05321e-08 0) + |Linear momentum| = 1.05321e-08 + Linear kinetic energy = 3.69464e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 388.812, 540.2 + Mass transfer phase change = 1.42645e-10 + D10, D32, Dmax (mu) = 63.8096, 88.5697, 160.545 + Liquid penetration 95% mass (m) = 0.0102594 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0283213, Final residual = 2.05773e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0502142, Final residual = 2.23656e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0021861, Final residual = 1.70124e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0011906, Final residual = 1.26471e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00119042, Final residual = 1.3946e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00119068, Final residual = 1.39773e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00208872, Final residual = 1.44669e-07, No Iterations 1 +min/max(T) = 726.548, 2819.7 +GAMG: Solving for p, Initial residual = 0.0164662, Final residual = 0.000878839, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.90454e-05, global = 1.06109e-05, cumulative = 0.00322784 +GAMG: Solving for p, Initial residual = 0.000847474, Final residual = 4.9935e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.30693e-05, global = 1.3066e-05, cumulative = 0.0032409 +smoothSolver: Solving for epsilon, Initial residual = 0.000981067, Final residual = 1.80624e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00144592, Final residual = 3.65212e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.109064 s +other Time = 1e-06 s +rho Equations = 0.000182 s +U Equations = 0.001302 s +Y Equations = 0.00257561 s +E Equations = 0.000643 s +p Equations = 0.002502 s +calculate parcels = 106.545 s +chemistry correctThermo = 0.002904 s +turbulence correct = 0.00104 s +combustion correct(in Y) = 0.0977174 s +percentage of chemistry = 89.5964 % +percentage of rho/U/Y/E = 4.31179 % +========Time details of each equation======= +rhoEqn Time = 0.000331 s +rhoEqn assamble = 0.000261 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.0013 s +UEqn assamble = 0.000781 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000519 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001845 s +YEqn assamble = 0.000652 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000178 s +YEqn correct boundary = 0 s +EEqn Time = 0.000485 s +EEqn assamble = 0.000363 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000122 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 160.24 s ClockTime = 161 s +Courant Number mean: 0.00475749 max: 0.0424838 +Time = 0.00142 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22412 + Current mass in system = 1.5624e-09 + Linear momentum = (1.98679e-11 -1.04956e-08 0) + |Linear momentum| = 1.04956e-08 + Linear kinetic energy = 3.67269e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 388.919, 540.2 + Mass transfer phase change = 1.43745e-10 + D10, D32, Dmax (mu) = 63.7564, 88.5485, 160.785 + Liquid penetration 95% mass (m) = 0.0102779 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0369556, Final residual = 2.7588e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0532147, Final residual = 2.29569e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00205935, Final residual = 1.51202e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00116817, Final residual = 1.17857e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00115145, Final residual = 1.28864e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00115164, Final residual = 1.29157e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00199893, Final residual = 1.35152e-07, No Iterations 1 +min/max(T) = 727.353, 2819.76 +GAMG: Solving for p, Initial residual = 0.0149444, Final residual = 0.000575904, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.72405e-05, global = 1.13447e-05, cumulative = 0.00325225 +GAMG: Solving for p, Initial residual = 0.000550118, Final residual = 2.99969e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.26797e-05, global = 1.26775e-05, cumulative = 0.00326493 +smoothSolver: Solving for epsilon, Initial residual = 0.000936565, Final residual = 1.67218e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00137181, Final residual = 3.34527e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097343 s +other Time = 0 s +rho Equations = 0.000171 s +U Equations = 0.001257 s +Y Equations = 0.00255242 s +E Equations = 0.000544 s +p Equations = 0.002469 s +calculate parcels = 106.897 s +chemistry correctThermo = 0.002094 s +turbulence correct = 0.001042 s +combustion correct(in Y) = 0.0870016 s +percentage of chemistry = 89.3763 % +percentage of rho/U/Y/E = 4.64792 % +========Time details of each equation======= +rhoEqn Time = 0.000333 s +rhoEqn assamble = 0.000266 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001257 s +UEqn assamble = 0.000752 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000505 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00189 s +YEqn assamble = 0.00064 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000236 s +YEqn correct boundary = 0 s +EEqn Time = 0.000403 s +EEqn assamble = 0.000303 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.0001 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 160.69 s ClockTime = 161 s +Courant Number mean: 0.00453594 max: 0.0412936 +Time = 0.0014225 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22412 + Current mass in system = 1.56132e-09 + Linear momentum = (2.05776e-11 -1.04616e-08 0) + |Linear momentum| = 1.04617e-08 + Linear kinetic energy = 3.65232e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 389.025, 540.2 + Mass transfer phase change = 1.44825e-10 + D10, D32, Dmax (mu) = 63.6473, 88.534, 161.026 + Liquid penetration 95% mass (m) = 0.0102964 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0405016, Final residual = 3.01661e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0566145, Final residual = 2.36041e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00202324, Final residual = 1.43449e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0011443, Final residual = 1.06948e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00112362, Final residual = 1.17261e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00112382, Final residual = 1.17542e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.001944, Final residual = 1.26969e-07, No Iterations 1 +min/max(T) = 728.389, 2819.56 +GAMG: Solving for p, Initial residual = 0.01395, Final residual = 0.000480932, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.60451e-05, global = 1.14757e-05, cumulative = 0.0032764 +GAMG: Solving for p, Initial residual = 0.00045709, Final residual = 1.87717e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.24439e-05, global = 1.24429e-05, cumulative = 0.00328885 +smoothSolver: Solving for epsilon, Initial residual = 0.000897599, Final residual = 1.56621e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00130484, Final residual = 3.07964e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092114 s +other Time = 0 s +rho Equations = 0.000182 s +U Equations = 0.001254 s +Y Equations = 0.00213149 s +E Equations = 0.000479 s +p Equations = 0.001907 s +calculate parcels = 107.259 s +chemistry correctThermo = 0.002047 s +turbulence correct = 0.000872 s +combustion correct(in Y) = 0.0830325 s +percentage of chemistry = 90.141 % +percentage of rho/U/Y/E = 4.39292 % +========Time details of each equation======= +rhoEqn Time = 0.000298 s +rhoEqn assamble = 0.000233 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001253 s +UEqn assamble = 0.000765 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000488 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001381 s +YEqn assamble = 0.000511 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 4.4e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000361 s +EEqn assamble = 0.000268 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 161.14 s ClockTime = 162 s +Courant Number mean: 0.00431714 max: 0.0395001 +Time = 0.001425 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22412 + Current mass in system = 1.56025e-09 + Linear momentum = (2.08328e-11 -1.04303e-08 0) + |Linear momentum| = 1.04303e-08 + Linear kinetic energy = 3.63365e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 389.136, 540.2 + Mass transfer phase change = 1.45897e-10 + D10, D32, Dmax (mu) = 63.547, 88.5281, 161.271 + Liquid penetration 95% mass (m) = 0.0103143 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0398165, Final residual = 2.85779e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0600363, Final residual = 2.40928e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00200736, Final residual = 1.39185e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00111816, Final residual = 9.96697e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00109607, Final residual = 1.10106e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00109629, Final residual = 1.10391e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00189541, Final residual = 1.21985e-07, No Iterations 1 +min/max(T) = 729.583, 2819.13 +GAMG: Solving for p, Initial residual = 0.0130839, Final residual = 0.000438019, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.54896e-05, global = 1.17042e-05, cumulative = 0.00330055 +GAMG: Solving for p, Initial residual = 0.000416168, Final residual = 2.08708e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.23563e-05, global = 1.23553e-05, cumulative = 0.00331291 +smoothSolver: Solving for epsilon, Initial residual = 0.000864251, Final residual = 1.4724e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00125527, Final residual = 2.86785e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.077049 s +other Time = 0 s +rho Equations = 0.00018 s +U Equations = 0.00125 s +Y Equations = 0.00240279 s +E Equations = 0.000628 s +p Equations = 0.002574 s +calculate parcels = 107.537 s +chemistry correctThermo = 0.002033 s +turbulence correct = 0.000911 s +combustion correct(in Y) = 0.0668652 s +percentage of chemistry = 86.7827 % +percentage of rho/U/Y/E = 5.78955 % +========Time details of each equation======= +rhoEqn Time = 0.000328 s +rhoEqn assamble = 0.000264 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001248 s +UEqn assamble = 0.000786 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000462 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001751 s +YEqn assamble = 0.0006 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000123 s +YEqn correct boundary = 0 s +EEqn Time = 0.000475 s +EEqn assamble = 0.000312 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000163 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 161.5 s ClockTime = 162 s +Courant Number mean: 0.00410127 max: 0.0376322 +Time = 0.0014275 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22411 + Current mass in system = 1.55916e-09 + Linear momentum = (2.07477e-11 -1.04009e-08 0) + |Linear momentum| = 1.04009e-08 + Linear kinetic energy = 3.61629e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 389.25, 540.2 + Mass transfer phase change = 1.46985e-10 + D10, D32, Dmax (mu) = 63.5019, 88.535, 161.481 + Liquid penetration 95% mass (m) = 0.0103317 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.034536, Final residual = 2.51694e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0629895, Final residual = 2.41047e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00201669, Final residual = 1.42631e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00108932, Final residual = 9.35504e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00106328, Final residual = 1.02501e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0010635, Final residual = 1.02761e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00185992, Final residual = 1.19541e-07, No Iterations 1 +min/max(T) = 730.836, 2818.56 +GAMG: Solving for p, Initial residual = 0.0125847, Final residual = 0.000412874, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.53841e-05, global = 1.19477e-05, cumulative = 0.00332485 +GAMG: Solving for p, Initial residual = 0.000392847, Final residual = 9.28265e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.25506e-05, global = 1.25457e-05, cumulative = 0.0033374 +smoothSolver: Solving for epsilon, Initial residual = 0.000844997, Final residual = 1.3769e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00122102, Final residual = 2.66478e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09034 s +other Time = 0 s +rho Equations = 0.000155 s +U Equations = 0.001121 s +Y Equations = 0.00203869 s +E Equations = 0.000486 s +p Equations = 0.001901 s +calculate parcels = 107.894 s +chemistry correctThermo = 0.002036 s +turbulence correct = 0.000853 s +combustion correct(in Y) = 0.0815763 s +percentage of chemistry = 90.2992 % +percentage of rho/U/Y/E = 4.2071 % +========Time details of each equation======= +rhoEqn Time = 0.000275 s +rhoEqn assamble = 0.000218 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00112 s +UEqn assamble = 0.000701 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000419 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001476 s +YEqn assamble = 0.000502 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000131 s +YEqn correct boundary = 0 s +EEqn Time = 0.000365 s +EEqn assamble = 0.000272 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 161.94 s ClockTime = 162 s +Courant Number mean: 0.00388623 max: 0.0361431 +Time = 0.00143 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22411 + Current mass in system = 1.55809e-09 + Linear momentum = (2.05309e-11 -1.03732e-08 0) + |Linear momentum| = 1.03732e-08 + Linear kinetic energy = 3.60002e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 389.366, 540.2 + Mass transfer phase change = 1.4805e-10 + D10, D32, Dmax (mu) = 63.4118, 88.5419, 161.662 + Liquid penetration 95% mass (m) = 0.0103486 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0328582, Final residual = 2.41016e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0659075, Final residual = 2.39646e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00191283, Final residual = 1.32946e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00105151, Final residual = 8.77156e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00102681, Final residual = 9.55033e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00102702, Final residual = 9.5754e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00181362, Final residual = 1.16533e-07, No Iterations 1 +min/max(T) = 732.13, 2817.81 +GAMG: Solving for p, Initial residual = 0.0121247, Final residual = 0.000353091, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.49552e-05, global = 1.18228e-05, cumulative = 0.00334922 +GAMG: Solving for p, Initial residual = 0.000335436, Final residual = 7.29401e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.22731e-05, global = 1.22673e-05, cumulative = 0.00336149 +smoothSolver: Solving for epsilon, Initial residual = 0.000813756, Final residual = 1.26182e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00116869, Final residual = 2.42312e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.101482 s +other Time = 1e-06 s +rho Equations = 0.000358 s +U Equations = 0.001744 s +Y Equations = 0.00273153 s +E Equations = 0.000577 s +p Equations = 0.002332 s +calculate parcels = 108.258 s +chemistry correctThermo = 0.002935 s +turbulence correct = 0.001116 s +combustion correct(in Y) = 0.0894545 s +percentage of chemistry = 88.1481 % +percentage of rho/U/Y/E = 5.33152 % +========Time details of each equation======= +rhoEqn Time = 0.000506 s +rhoEqn assamble = 0.000398 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000108 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001742 s +UEqn assamble = 0.001052 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00069 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001618 s +YEqn assamble = 0.000647 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -6.4e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000426 s +EEqn assamble = 0.000316 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00011 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 162.41 s ClockTime = 163 s +Courant Number mean: 0.00366985 max: 0.0345662 +Time = 0.0014325 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22410 + Current mass in system = 1.55703e-09 + Linear momentum = (2.02606e-11 -1.03472e-08 0) + |Linear momentum| = 1.03472e-08 + Linear kinetic energy = 3.58484e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 389.483, 540.2 + Mass transfer phase change = 1.49114e-10 + D10, D32, Dmax (mu) = 63.4233, 88.5606, 161.847 + Liquid penetration 95% mass (m) = 0.0103654 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.033664, Final residual = 2.38399e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0696339, Final residual = 2.43337e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00186601, Final residual = 1.30599e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00101287, Final residual = 8.23817e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000983167, Final residual = 8.92338e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000983379, Final residual = 8.94753e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00177788, Final residual = 1.14557e-07, No Iterations 1 +min/max(T) = 733.533, 2817.01 +GAMG: Solving for p, Initial residual = 0.0114543, Final residual = 0.000304122, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.46695e-05, global = 1.17904e-05, cumulative = 0.00337328 +GAMG: Solving for p, Initial residual = 0.000289865, Final residual = 5.34902e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.22749e-05, global = 1.2271e-05, cumulative = 0.00338555 +smoothSolver: Solving for epsilon, Initial residual = 0.000770893, Final residual = 1.13669e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00110595, Final residual = 2.16618e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.112737 s +other Time = 1e-06 s +rho Equations = 0.00018 s +U Equations = 0.001204 s +Y Equations = 0.00246895 s +E Equations = 0.000597 s +p Equations = 0.00243 s +calculate parcels = 108.612 s +chemistry correctThermo = 0.002961 s +turbulence correct = 0.001124 s +combustion correct(in Y) = 0.101556 s +percentage of chemistry = 90.0823 % +percentage of rho/U/Y/E = 3.94719 % +========Time details of each equation======= +rhoEqn Time = 0.000353 s +rhoEqn assamble = 0.000279 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001202 s +UEqn assamble = 0.0007 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000502 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001823 s +YEqn assamble = 0.000662 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000185 s +YEqn correct boundary = 0 s +EEqn Time = 0.000438 s +EEqn assamble = 0.000321 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 162.88 s ClockTime = 163 s +Courant Number mean: 0.00345145 max: 0.0328813 +Time = 0.001435 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22408 + Current mass in system = 1.55594e-09 + Linear momentum = (2.00259e-11 -1.0323e-08 0) + |Linear momentum| = 1.0323e-08 + Linear kinetic energy = 3.57087e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 389.599, 540.2 + Mass transfer phase change = 1.50202e-10 + D10, D32, Dmax (mu) = 63.4237, 88.5947, 162.423 + Liquid penetration 95% mass (m) = 0.0103825 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0359422, Final residual = 2.42498e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0742141, Final residual = 2.52336e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00188118, Final residual = 1.37928e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000980045, Final residual = 7.75329e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000946341, Final residual = 8.33241e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000946551, Final residual = 8.35576e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00175347, Final residual = 1.149e-07, No Iterations 1 +min/max(T) = 735.072, 2816.2 +GAMG: Solving for p, Initial residual = 0.0108524, Final residual = 0.000275214, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.45912e-05, global = 1.21575e-05, cumulative = 0.00339771 +GAMG: Solving for p, Initial residual = 0.000261984, Final residual = 7.98912e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.25374e-05, global = 1.25325e-05, cumulative = 0.00341024 +smoothSolver: Solving for epsilon, Initial residual = 0.0007307, Final residual = 1.03056e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00105013, Final residual = 1.94735e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.112145 s +other Time = 1e-06 s +rho Equations = 0.00018 s +U Equations = 0.001232 s +Y Equations = 0.00265292 s +E Equations = 0.000654 s +p Equations = 0.002443 s +calculate parcels = 108.994 s +chemistry correctThermo = 0.002963 s +turbulence correct = 0.001165 s +combustion correct(in Y) = 0.100653 s +percentage of chemistry = 89.7526 % +percentage of rho/U/Y/E = 4.20787 % +========Time details of each equation======= +rhoEqn Time = 0.000334 s +rhoEqn assamble = 0.000261 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001231 s +UEqn assamble = 0.000724 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000507 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002001 s +YEqn assamble = 0.000671 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000237 s +YEqn correct boundary = 0 s +EEqn Time = 0.000489 s +EEqn assamble = 0.000351 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000138 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 163.37 s ClockTime = 164 s +Courant Number mean: 0.00323568 max: 0.0313813 +Time = 0.0014375 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22404 + Current mass in system = 1.55483e-09 + Linear momentum = (1.98842e-11 -1.03004e-08 0) + |Linear momentum| = 1.03004e-08 + Linear kinetic energy = 3.55802e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 389.706, 540.2 + Mass transfer phase change = 1.51311e-10 + D10, D32, Dmax (mu) = 63.604, 88.6434, 163.21 + Liquid penetration 95% mass (m) = 0.0104 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.038727, Final residual = 2.48318e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0785387, Final residual = 2.58824e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00188249, Final residual = 1.4367e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000957234, Final residual = 7.41189e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000928711, Final residual = 8.09162e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000928878, Final residual = 8.11511e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00172591, Final residual = 1.16134e-07, No Iterations 1 +min/max(T) = 736.758, 2815.35 +GAMG: Solving for p, Initial residual = 0.0105155, Final residual = 0.000357033, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.52301e-05, global = 1.22111e-05, cumulative = 0.00342245 +GAMG: Solving for p, Initial residual = 0.000344437, Final residual = 2.42969e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.2789e-05, global = 1.27877e-05, cumulative = 0.00343524 +smoothSolver: Solving for epsilon, Initial residual = 0.000720862, Final residual = 9.75986e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00102046, Final residual = 1.80751e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.083111 s +other Time = 0 s +rho Equations = 0.000172 s +U Equations = 0.001126 s +Y Equations = 0.00217357 s +E Equations = 0.000501 s +p Equations = 0.002114 s +calculate parcels = 109.315 s +chemistry correctThermo = 0.002069 s +turbulence correct = 0.000879 s +combustion correct(in Y) = 0.0738824 s +percentage of chemistry = 88.8961 % +percentage of rho/U/Y/E = 4.77984 % +========Time details of each equation======= +rhoEqn Time = 0.00032 s +rhoEqn assamble = 0.000243 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001126 s +UEqn assamble = 0.00071 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000416 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001594 s +YEqn assamble = 0.000556 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000141 s +YEqn correct boundary = 0 s +EEqn Time = 0.000378 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 163.78 s ClockTime = 164 s +Courant Number mean: 0.00302733 max: 0.0304116 +Time = 0.00144 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22404 + Current mass in system = 1.5538e-09 + Linear momentum = (1.99691e-11 -1.02794e-08 0) + |Linear momentum| = 1.02794e-08 + Linear kinetic energy = 3.54604e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 389.81, 540.2 + Mass transfer phase change = 1.52339e-10 + D10, D32, Dmax (mu) = 63.5373, 88.6748, 163.973 + Liquid penetration 95% mass (m) = 0.0104174 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0396728, Final residual = 2.31921e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0818208, Final residual = 2.59752e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00174364, Final residual = 1.30345e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000932263, Final residual = 7.23119e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000897162, Final residual = 7.83645e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000897314, Final residual = 7.85954e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00168592, Final residual = 1.14505e-07, No Iterations 1 +min/max(T) = 738.536, 2814.39 +GAMG: Solving for p, Initial residual = 0.0102081, Final residual = 0.000386338, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.47446e-05, global = 1.12573e-05, cumulative = 0.0034465 +GAMG: Solving for p, Initial residual = 0.000371826, Final residual = 2.95792e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.1852e-05, global = 1.18497e-05, cumulative = 0.00345835 +smoothSolver: Solving for epsilon, Initial residual = 0.000694089, Final residual = 9.17924e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000986273, Final residual = 1.68067e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102613 s +other Time = 1e-06 s +rho Equations = 0.000163 s +U Equations = 0.001098 s +Y Equations = 0.00242648 s +E Equations = 0.00061 s +p Equations = 0.002345 s +calculate parcels = 109.617 s +chemistry correctThermo = 0.002831 s +turbulence correct = 0.000945 s +combustion correct(in Y) = 0.0918865 s +percentage of chemistry = 89.5467 % +percentage of rho/U/Y/E = 4.18805 % +========Time details of each equation======= +rhoEqn Time = 0.000302 s +rhoEqn assamble = 0.000232 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001098 s +UEqn assamble = 0.000667 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000431 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001862 s +YEqn assamble = 0.000652 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00024 s +YEqn correct boundary = 0 s +EEqn Time = 0.000451 s +EEqn assamble = 0.000325 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000126 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 164.18 s ClockTime = 165 s +Courant Number mean: 0.00280679 max: 0.0291502 +Time = 0.0014425 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22404 + Current mass in system = 1.55278e-09 + Linear momentum = (2.00464e-11 -1.02595e-08 0) + |Linear momentum| = 1.02595e-08 + Linear kinetic energy = 3.53472e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 389.927, 540.2 + Mass transfer phase change = 1.5336e-10 + D10, D32, Dmax (mu) = 63.4711, 88.7076, 164.695 + Liquid penetration 95% mass (m) = 0.0104357 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0401844, Final residual = 2.22851e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0845718, Final residual = 2.58629e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00171389, Final residual = 1.28166e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000901433, Final residual = 6.76191e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000866669, Final residual = 7.36724e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000866835, Final residual = 7.39003e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00163586, Final residual = 1.10963e-07, No Iterations 1 +min/max(T) = 740.393, 2813.31 +GAMG: Solving for p, Initial residual = 0.00946727, Final residual = 0.000272822, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.38506e-05, global = 1.1438e-05, cumulative = 0.00346978 +GAMG: Solving for p, Initial residual = 0.000262414, Final residual = 6.99258e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.17709e-05, global = 1.17656e-05, cumulative = 0.00348155 +smoothSolver: Solving for epsilon, Initial residual = 0.000680716, Final residual = 8.86006e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000970913, Final residual = 1.60535e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103033 s +other Time = 1e-06 s +rho Equations = 0.000309 s +U Equations = 0.001868 s +Y Equations = 0.00236058 s +E Equations = 0.000548 s +p Equations = 0.00225 s +calculate parcels = 109.975 s +chemistry correctThermo = 0.002861 s +turbulence correct = 0.001065 s +combustion correct(in Y) = 0.0915054 s +percentage of chemistry = 88.8118 % +percentage of rho/U/Y/E = 4.93588 % +========Time details of each equation======= +rhoEqn Time = 0.000459 s +rhoEqn assamble = 0.000349 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.00011 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001866 s +UEqn assamble = 0.00108 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000786 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001271 s +YEqn assamble = 0.000534 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -0.000104 s +YEqn correct boundary = 0 s +EEqn Time = 0.000431 s +EEqn assamble = 0.000313 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 164.64 s ClockTime = 165 s +Courant Number mean: 0.00258756 max: 0.0278792 +Time = 0.001445 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22404 + Current mass in system = 1.55177e-09 + Linear momentum = (2.00557e-11 -1.02402e-08 0) + |Linear momentum| = 1.02403e-08 + Linear kinetic energy = 3.5239e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 390.052, 540.2 + Mass transfer phase change = 1.54376e-10 + D10, D32, Dmax (mu) = 63.4071, 88.7413, 164.952 + Liquid penetration 95% mass (m) = 0.010453 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0421854, Final residual = 2.15913e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.087095, Final residual = 2.56235e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00168926, Final residual = 1.25632e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00087913, Final residual = 6.39582e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000845205, Final residual = 7.04541e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000845411, Final residual = 7.06694e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00158859, Final residual = 1.07837e-07, No Iterations 1 +min/max(T) = 742.331, 2812.19 +GAMG: Solving for p, Initial residual = 0.00885862, Final residual = 0.000213283, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.33035e-05, global = 1.1434e-05, cumulative = 0.00349298 +GAMG: Solving for p, Initial residual = 0.000205077, Final residual = 5.16887e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.17087e-05, global = 1.1705e-05, cumulative = 0.00350469 +smoothSolver: Solving for epsilon, Initial residual = 0.000670077, Final residual = 8.56365e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000961307, Final residual = 1.54839e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095042 s +other Time = 1e-06 s +rho Equations = 0.000245 s +U Equations = 0.00176 s +Y Equations = 0.00250961 s +E Equations = 0.000499 s +p Equations = 0.001916 s +calculate parcels = 110.291 s +chemistry correctThermo = 0.002048 s +turbulence correct = 0.000896 s +combustion correct(in Y) = 0.0849304 s +percentage of chemistry = 89.3609 % +percentage of rho/U/Y/E = 5.27516 % +========Time details of each equation======= +rhoEqn Time = 0.00037 s +rhoEqn assamble = 0.000273 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001758 s +UEqn assamble = 0.001 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000758 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001436 s +YEqn assamble = 0.000554 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -9.2e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000372 s +EEqn assamble = 0.000278 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 165.05 s ClockTime = 166 s +Courant Number mean: 0.00237238 max: 0.0265477 +Time = 0.0014475 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22402 + Current mass in system = 1.55071e-09 + Linear momentum = (1.99776e-11 -1.02213e-08 0) + |Linear momentum| = 1.02213e-08 + Linear kinetic energy = 3.51335e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 390.18, 540.2 + Mass transfer phase change = 1.55436e-10 + D10, D32, Dmax (mu) = 63.3854, 88.7855, 164.784 + Liquid penetration 95% mass (m) = 0.0104708 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0407857, Final residual = 1.95581e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0891033, Final residual = 2.5312e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00176506, Final residual = 1.39599e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000864283, Final residual = 6.17785e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000836258, Final residual = 6.94601e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000836477, Final residual = 6.96713e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0015564, Final residual = 1.05954e-07, No Iterations 1 +min/max(T) = 744.357, 2811.06 +GAMG: Solving for p, Initial residual = 0.00864202, Final residual = 0.000241376, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.37088e-05, global = 1.17492e-05, cumulative = 0.00351644 +GAMG: Solving for p, Initial residual = 0.000233887, Final residual = 9.82475e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.22226e-05, global = 1.22176e-05, cumulative = 0.00352866 +smoothSolver: Solving for epsilon, Initial residual = 0.000650376, Final residual = 8.19941e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000945973, Final residual = 1.4829e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.104118 s +other Time = 1e-06 s +rho Equations = 0.00017 s +U Equations = 0.00115 s +Y Equations = 0.00242832 s +E Equations = 0.000594 s +p Equations = 0.002301 s +calculate parcels = 110.651 s +chemistry correctThermo = 0.002839 s +turbulence correct = 0.001027 s +combustion correct(in Y) = 0.0934107 s +percentage of chemistry = 89.7162 % +percentage of rho/U/Y/E = 4.17057 % +========Time details of each equation======= +rhoEqn Time = 0.000317 s +rhoEqn assamble = 0.000252 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001149 s +UEqn assamble = 0.000652 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000497 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001789 s +YEqn assamble = 0.000619 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000199 s +YEqn correct boundary = 0 s +EEqn Time = 0.000443 s +EEqn assamble = 0.000331 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 165.52 s ClockTime = 166 s +Courant Number mean: 0.00216944 max: 0.02552 +Time = 0.00145 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22398 + Current mass in system = 1.54959e-09 + Linear momentum = (1.98051e-11 -1.02024e-08 0) + |Linear momentum| = 1.02024e-08 + Linear kinetic energy = 3.50292e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 390.302, 540.2 + Mass transfer phase change = 1.56552e-10 + D10, D32, Dmax (mu) = 63.4318, 88.84, 164.44 + Liquid penetration 95% mass (m) = 0.010489 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0354485, Final residual = 1.67155e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0909376, Final residual = 2.48313e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00184387, Final residual = 1.47965e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00085634, Final residual = 6.07181e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000824577, Final residual = 6.77768e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000824812, Final residual = 6.79859e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00154037, Final residual = 1.04567e-07, No Iterations 1 +min/max(T) = 746.463, 2809.87 +GAMG: Solving for p, Initial residual = 0.00874199, Final residual = 0.000327805, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.50604e-05, global = 1.20224e-05, cumulative = 0.00354068 +GAMG: Solving for p, Initial residual = 0.000320462, Final residual = 2.35582e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.28665e-05, global = 1.28654e-05, cumulative = 0.00355354 +smoothSolver: Solving for epsilon, Initial residual = 0.000657613, Final residual = 8.09517e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000949043, Final residual = 1.45596e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.104484 s +other Time = 1e-06 s +rho Equations = 0.000145 s +U Equations = 0.000973 s +Y Equations = 0.00238771 s +E Equations = 0.000495 s +p Equations = 0.002051 s +calculate parcels = 111.021 s +chemistry correctThermo = 0.002032 s +turbulence correct = 0.001055 s +combustion correct(in Y) = 0.0951673 s +percentage of chemistry = 91.0831 % +percentage of rho/U/Y/E = 3.82901 % +========Time details of each equation======= +rhoEqn Time = 0.000268 s +rhoEqn assamble = 0.000212 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000972 s +UEqn assamble = 0.000559 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000413 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001842 s +YEqn assamble = 0.000619 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000212 s +YEqn correct boundary = 0 s +EEqn Time = 0.00037 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 165.99 s ClockTime = 167 s +Courant Number mean: 0.00197333 max: 0.024554 +Time = 0.0014525 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22396 + Current mass in system = 1.54855e-09 + Linear momentum = (1.96558e-11 -1.01837e-08 0) + |Linear momentum| = 1.01837e-08 + Linear kinetic energy = 3.49252e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 390.404, 540.2 + Mass transfer phase change = 1.57595e-10 + D10, D32, Dmax (mu) = 63.6289, 88.8817, 164.093 + Liquid penetration 95% mass (m) = 0.0105048 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0320536, Final residual = 1.31695e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.092812, Final residual = 2.44901e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00169385, Final residual = 1.19893e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000843894, Final residual = 5.97191e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000806847, Final residual = 6.57869e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000807017, Final residual = 6.5989e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00151092, Final residual = 9.99645e-08, No Iterations 1 +min/max(T) = 748.632, 2808.55 +GAMG: Solving for p, Initial residual = 0.0087076, Final residual = 0.000326746, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.44e-05, global = 1.14766e-05, cumulative = 0.00356502 +GAMG: Solving for p, Initial residual = 0.000315427, Final residual = 2.81425e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.20204e-05, global = 1.20183e-05, cumulative = 0.00357704 +smoothSolver: Solving for epsilon, Initial residual = 0.000660319, Final residual = 8.05589e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000949939, Final residual = 1.43514e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.075404 s +other Time = 1e-06 s +rho Equations = 0.00021 s +U Equations = 0.001103 s +Y Equations = 0.00228722 s +E Equations = 0.000496 s +p Equations = 0.002039 s +calculate parcels = 111.295 s +chemistry correctThermo = 0.001951 s +turbulence correct = 0.000982 s +combustion correct(in Y) = 0.0660208 s +percentage of chemistry = 87.5561 % +percentage of rho/U/Y/E = 5.43237 % +========Time details of each equation======= +rhoEqn Time = 0.000329 s +rhoEqn assamble = 0.000263 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001103 s +UEqn assamble = 0.000678 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000425 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001721 s +YEqn assamble = 0.000656 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000161 s +YEqn correct boundary = 0 s +EEqn Time = 0.000374 s +EEqn assamble = 0.00028 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 166.34 s ClockTime = 167 s +Courant Number mean: 0.00176997 max: 0.0234926 +Time = 0.001455 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22395 + Current mass in system = 1.54751e-09 + Linear momentum = (1.9438e-11 -1.0165e-08 0) + |Linear momentum| = 1.0165e-08 + Linear kinetic energy = 3.48209e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 390.528, 540.2 + Mass transfer phase change = 1.58629e-10 + D10, D32, Dmax (mu) = 63.7081, 88.9167, 163.779 + Liquid penetration 95% mass (m) = 0.0105224 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0271573, Final residual = 1.04912e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0942504, Final residual = 2.42267e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0016508, Final residual = 1.14205e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00081975, Final residual = 5.69879e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000785358, Final residual = 6.35663e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000785539, Final residual = 6.37651e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0014814, Final residual = 9.58842e-08, No Iterations 1 +min/max(T) = 750.839, 2807.11 +GAMG: Solving for p, Initial residual = 0.00837134, Final residual = 0.000228051, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.35688e-05, global = 1.16984e-05, cumulative = 0.00358874 +GAMG: Solving for p, Initial residual = 0.000221138, Final residual = 6.58883e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.19278e-05, global = 1.19234e-05, cumulative = 0.00360066 +smoothSolver: Solving for epsilon, Initial residual = 0.000662305, Final residual = 7.98234e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000948483, Final residual = 1.40738e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.105324 s +other Time = 0 s +rho Equations = 0.000179 s +U Equations = 0.001194 s +Y Equations = 0.00252193 s +E Equations = 0.000688 s +p Equations = 0.001802 s +calculate parcels = 111.649 s +chemistry correctThermo = 0.002484 s +turbulence correct = 0.000815 s +combustion correct(in Y) = 0.0954321 s +percentage of chemistry = 90.6081 % +percentage of rho/U/Y/E = 4.35126 % +========Time details of each equation======= +rhoEqn Time = 0.000297 s +rhoEqn assamble = 0.000236 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001192 s +UEqn assamble = 0.000689 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000503 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001869 s +YEqn assamble = 0.000639 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000178 s +YEqn correct boundary = 0 s +EEqn Time = 0.000529 s +EEqn assamble = 0.000356 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000173 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 166.8 s ClockTime = 167 s +Courant Number mean: 0.00157121 max: 0.0222644 +Time = 0.0014575 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22394 + Current mass in system = 1.54647e-09 + Linear momentum = (1.91858e-11 -1.01461e-08 0) + |Linear momentum| = 1.01462e-08 + Linear kinetic energy = 3.47162e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 390.665, 540.2 + Mass transfer phase change = 1.59676e-10 + D10, D32, Dmax (mu) = 63.7683, 88.9544, 164.033 + Liquid penetration 95% mass (m) = 0.0105387 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0206013, Final residual = 7.77973e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0955452, Final residual = 2.3884e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00165369, Final residual = 1.1034e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000802367, Final residual = 5.53384e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000766671, Final residual = 6.15449e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000766881, Final residual = 6.17366e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00146486, Final residual = 9.33284e-08, No Iterations 1 +min/max(T) = 753.107, 2805.72 +GAMG: Solving for p, Initial residual = 0.00822799, Final residual = 0.000209232, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.34917e-05, global = 1.18521e-05, cumulative = 0.00361251 +GAMG: Solving for p, Initial residual = 0.000202383, Final residual = 5.80327e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.20749e-05, global = 1.20715e-05, cumulative = 0.00362458 +smoothSolver: Solving for epsilon, Initial residual = 0.000658723, Final residual = 7.8006e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000941246, Final residual = 1.36664e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102872 s +other Time = 0 s +rho Equations = 0.000199 s +U Equations = 0.001309 s +Y Equations = 0.0022181 s +E Equations = 0.000485 s +p Equations = 0.002338 s +calculate parcels = 112.007 s +chemistry correctThermo = 0.002028 s +turbulence correct = 0.001103 s +combustion correct(in Y) = 0.0929949 s +percentage of chemistry = 90.3987 % +percentage of rho/U/Y/E = 4.09353 % +========Time details of each equation======= +rhoEqn Time = 0.000354 s +rhoEqn assamble = 0.000278 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001308 s +UEqn assamble = 0.000753 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000555 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00143 s +YEqn assamble = 0.00053 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 6.3e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000365 s +EEqn assamble = 0.000271 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 167.26 s ClockTime = 168 s +Courant Number mean: 0.0013752 max: 0.0209579 +Time = 0.00146 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22394 + Current mass in system = 1.54542e-09 + Linear momentum = (1.89724e-11 -1.01272e-08 0) + |Linear momentum| = 1.01273e-08 + Linear kinetic energy = 3.46113e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 390.806, 540.2 + Mass transfer phase change = 1.60723e-10 + D10, D32, Dmax (mu) = 63.7015, 88.9873, 164.298 + Liquid penetration 95% mass (m) = 0.010556 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0187471, Final residual = 6.82649e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0966799, Final residual = 2.35303e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00162594, Final residual = 1.06752e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000787365, Final residual = 5.39823e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000753096, Final residual = 5.98569e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000753323, Final residual = 6.00449e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00145146, Final residual = 9.105e-08, No Iterations 1 +min/max(T) = 755.455, 2804.42 +GAMG: Solving for p, Initial residual = 0.00821116, Final residual = 0.000184219, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.34043e-05, global = 1.1871e-05, cumulative = 0.00363645 +GAMG: Solving for p, Initial residual = 0.00017875, Final residual = 3.92533e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.20625e-05, global = 1.20602e-05, cumulative = 0.00364851 +smoothSolver: Solving for epsilon, Initial residual = 0.000654921, Final residual = 7.67754e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000932787, Final residual = 1.33166e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102744 s +other Time = 0 s +rho Equations = 0.000159 s +U Equations = 0.001141 s +Y Equations = 0.00226789 s +E Equations = 0.000613 s +p Equations = 0.002322 s +calculate parcels = 112.378 s +chemistry correctThermo = 0.0029 s +turbulence correct = 0.00113 s +combustion correct(in Y) = 0.0920291 s +percentage of chemistry = 89.5713 % +percentage of rho/U/Y/E = 4.06923 % +========Time details of each equation======= +rhoEqn Time = 0.000301 s +rhoEqn assamble = 0.000239 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001139 s +UEqn assamble = 0.000618 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000521 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001528 s +YEqn assamble = 0.000582 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 7.7e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000451 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 167.74 s ClockTime = 168 s +Courant Number mean: 0.00126477 max: 0.019729 +Time = 0.0014625 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22391 + Current mass in system = 1.54434e-09 + Linear momentum = (1.88067e-11 -1.01082e-08 0) + |Linear momentum| = 1.01082e-08 + Linear kinetic energy = 3.45063e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 390.947, 540.2 + Mass transfer phase change = 1.61801e-10 + D10, D32, Dmax (mu) = 63.8448, 89.0281, 164.574 + Liquid penetration 95% mass (m) = 0.0105745 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.021915, Final residual = 7.20229e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0977743, Final residual = 2.3383e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00165408, Final residual = 1.0795e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000777112, Final residual = 5.30747e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000738689, Final residual = 5.80268e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000738914, Final residual = 5.82096e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00144496, Final residual = 8.96949e-08, No Iterations 1 +min/max(T) = 757.882, 2803.17 +GAMG: Solving for p, Initial residual = 0.00868375, Final residual = 0.00018072, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.36114e-05, global = 1.22508e-05, cumulative = 0.00366077 +GAMG: Solving for p, Initial residual = 0.000176083, Final residual = 6.41558e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.24319e-05, global = 1.24289e-05, cumulative = 0.00367319 +smoothSolver: Solving for epsilon, Initial residual = 0.000654, Final residual = 7.55575e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000926907, Final residual = 1.30611e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097716 s +other Time = 1e-06 s +rho Equations = 0.000517 s +U Equations = 0.001779 s +Y Equations = 0.00214752 s +E Equations = 0.000488 s +p Equations = 0.002027 s +calculate parcels = 112.722 s +chemistry correctThermo = 0.002058 s +turbulence correct = 0.00094 s +combustion correct(in Y) = 0.0875285 s +percentage of chemistry = 89.5744 % +percentage of rho/U/Y/E = 5.04679 % +========Time details of each equation======= +rhoEqn Time = 0.000639 s +rhoEqn assamble = 0.00053 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000109 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001778 s +UEqn assamble = 0.001269 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000509 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001494 s +YEqn assamble = 0.000556 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.4e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000364 s +EEqn assamble = 0.000271 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 168.18 s ClockTime = 169 s +Courant Number mean: 0.00125308 max: 0.0186009 +Time = 0.001465 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22388 + Current mass in system = 1.54324e-09 + Linear momentum = (1.869e-11 -1.00891e-08 0) + |Linear momentum| = 1.00891e-08 + Linear kinetic energy = 3.44013e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 391.082, 540.2 + Mass transfer phase change = 1.62899e-10 + D10, D32, Dmax (mu) = 64.0244, 89.0727, 164.862 + Liquid penetration 95% mass (m) = 0.0105928 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0243428, Final residual = 8.34043e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0988303, Final residual = 2.34672e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00168353, Final residual = 1.07803e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000765098, Final residual = 5.18942e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000725196, Final residual = 5.61007e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000725425, Final residual = 5.62792e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00145063, Final residual = 8.91672e-08, No Iterations 1 +min/max(T) = 760.349, 2801.92 +GAMG: Solving for p, Initial residual = 0.00948019, Final residual = 0.000181535, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.37652e-05, global = 1.25141e-05, cumulative = 0.00368571 +GAMG: Solving for p, Initial residual = 0.000177065, Final residual = 4.60402e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.2656e-05, global = 1.26535e-05, cumulative = 0.00369836 +smoothSolver: Solving for epsilon, Initial residual = 0.000655202, Final residual = 7.51762e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000923506, Final residual = 1.29032e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.075632 s +other Time = 0 s +rho Equations = 0.000172 s +U Equations = 0.001059 s +Y Equations = 0.00220615 s +E Equations = 0.000501 s +p Equations = 0.002074 s +calculate parcels = 113.056 s +chemistry correctThermo = 0.001926 s +turbulence correct = 0.000832 s +combustion correct(in Y) = 0.0666379 s +percentage of chemistry = 88.108 % +percentage of rho/U/Y/E = 5.20699 % +========Time details of each equation======= +rhoEqn Time = 0.000329 s +rhoEqn assamble = 0.000259 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001057 s +UEqn assamble = 0.000642 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000415 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001612 s +YEqn assamble = 0.000532 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000172 s +YEqn correct boundary = 0 s +EEqn Time = 0.000374 s +EEqn assamble = 0.000281 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 168.59 s ClockTime = 169 s +Courant Number mean: 0.00126633 max: 0.0175068 +Time = 0.0014675 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22388 + Current mass in system = 1.54218e-09 + Linear momentum = (1.86241e-11 -1.00702e-08 0) + |Linear momentum| = 1.00702e-08 + Linear kinetic energy = 3.42966e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 391.218, 540.2 + Mass transfer phase change = 1.63966e-10 + D10, D32, Dmax (mu) = 63.9544, 89.1041, 165.326 + Liquid penetration 95% mass (m) = 0.0106091 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0262994, Final residual = 9.97167e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0996257, Final residual = 2.36827e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00161333, Final residual = 9.87729e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000749101, Final residual = 5.04414e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000717403, Final residual = 5.53613e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000717648, Final residual = 5.55396e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00144992, Final residual = 8.71979e-08, No Iterations 1 +min/max(T) = 762.876, 2800.61 +GAMG: Solving for p, Initial residual = 0.0102024, Final residual = 0.000184066, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.35741e-05, global = 1.21868e-05, cumulative = 0.00371055 +GAMG: Solving for p, Initial residual = 0.00018024, Final residual = 7.39532e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.23065e-05, global = 1.23015e-05, cumulative = 0.00372285 +smoothSolver: Solving for epsilon, Initial residual = 0.000660882, Final residual = 7.5309e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000920975, Final residual = 1.27922e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.112328 s +other Time = 0 s +rho Equations = 0.000194 s +U Equations = 0.001267 s +Y Equations = 0.00218001 s +E Equations = 0.000524 s +p Equations = 0.002866 s +calculate parcels = 113.346 s +chemistry correctThermo = 0.002179 s +turbulence correct = 0.001211 s +combustion correct(in Y) = 0.101671 s +percentage of chemistry = 90.5126 % +percentage of rho/U/Y/E = 3.7079 % +========Time details of each equation======= +rhoEqn Time = 0.000392 s +rhoEqn assamble = 0.000304 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001266 s +UEqn assamble = 0.000752 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000514 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00153 s +YEqn assamble = 0.000545 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000123 s +YEqn correct boundary = 0 s +EEqn Time = 0.000399 s +EEqn assamble = 0.000282 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 168.99 s ClockTime = 170 s +Courant Number mean: 0.00129012 max: 0.0178663 +Time = 0.00147 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22388 + Current mass in system = 1.5411e-09 + Linear momentum = (1.85929e-11 -1.00512e-08 0) + |Linear momentum| = 1.00512e-08 + Linear kinetic energy = 3.41919e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 391.363, 540.2 + Mass transfer phase change = 1.6504e-10 + D10, D32, Dmax (mu) = 63.8842, 89.1362, 165.479 + Liquid penetration 95% mass (m) = 0.010625 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0277945, Final residual = 1.04118e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.100003, Final residual = 2.37615e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00160509, Final residual = 9.70949e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00073283, Final residual = 4.95369e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000703638, Final residual = 5.43826e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00070386, Final residual = 5.45509e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00144968, Final residual = 8.59801e-08, No Iterations 1 +min/max(T) = 765.471, 2799.3 +GAMG: Solving for p, Initial residual = 0.011081, Final residual = 0.000163054, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.34432e-05, global = 1.22688e-05, cumulative = 0.00373512 +GAMG: Solving for p, Initial residual = 0.000160163, Final residual = 3.03051e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.23795e-05, global = 1.23774e-05, cumulative = 0.0037475 +smoothSolver: Solving for epsilon, Initial residual = 0.000662353, Final residual = 7.49262e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000918194, Final residual = 1.268e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103558 s +other Time = 0 s +rho Equations = 0.000204 s +U Equations = 0.001372 s +Y Equations = 0.00251452 s +E Equations = 0.000639 s +p Equations = 0.002406 s +calculate parcels = 113.718 s +chemistry correctThermo = 0.002882 s +turbulence correct = 0.001078 s +combustion correct(in Y) = 0.0922455 s +percentage of chemistry = 89.0761 % +percentage of rho/U/Y/E = 4.56703 % +========Time details of each equation======= +rhoEqn Time = 0.000355 s +rhoEqn assamble = 0.000278 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00137 s +UEqn assamble = 0.000838 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000532 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001853 s +YEqn assamble = 0.00067 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000196 s +YEqn correct boundary = 0 s +EEqn Time = 0.000481 s +EEqn assamble = 0.000358 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000123 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 169.47 s ClockTime = 170 s +Courant Number mean: 0.00132166 max: 0.0180845 +Time = 0.0014725 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22387 + Current mass in system = 1.54e-09 + Linear momentum = (1.85894e-11 -1.0032e-08 0) + |Linear momentum| = 1.0032e-08 + Linear kinetic energy = 3.40871e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 391.513, 540.2 + Mass transfer phase change = 1.66147e-10 + D10, D32, Dmax (mu) = 63.856, 89.1746, 165.809 + Liquid penetration 95% mass (m) = 0.0106423 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0283211, Final residual = 1.11587e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0999556, Final residual = 2.37971e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00163522, Final residual = 9.87229e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000718239, Final residual = 4.85435e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000685508, Final residual = 5.24246e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000685733, Final residual = 5.25829e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00145688, Final residual = 8.49266e-08, No Iterations 1 +min/max(T) = 768.143, 2798.01 +GAMG: Solving for p, Initial residual = 0.0118835, Final residual = 0.000168583, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.37285e-05, global = 1.26172e-05, cumulative = 0.00376011 +GAMG: Solving for p, Initial residual = 0.000165861, Final residual = 5.1845e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.27599e-05, global = 1.27574e-05, cumulative = 0.00377287 +smoothSolver: Solving for epsilon, Initial residual = 0.000659114, Final residual = 7.38005e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000914519, Final residual = 1.25582e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.099286 s +other Time = 1e-06 s +rho Equations = 0.00018 s +U Equations = 0.001165 s +Y Equations = 0.00252275 s +E Equations = 0.000606 s +p Equations = 0.002189 s +calculate parcels = 114.069 s +chemistry correctThermo = 0.002866 s +turbulence correct = 0.001012 s +combustion correct(in Y) = 0.0884873 s +percentage of chemistry = 89.1236 % +percentage of rho/U/Y/E = 4.50592 % +========Time details of each equation======= +rhoEqn Time = 0.000323 s +rhoEqn assamble = 0.000252 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001165 s +UEqn assamble = 0.000676 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000489 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001884 s +YEqn assamble = 0.000684 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000203 s +YEqn correct boundary = 0 s +EEqn Time = 0.000448 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 169.92 s ClockTime = 170 s +Courant Number mean: 0.00136431 max: 0.0172107 +Time = 0.001475 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22387 + Current mass in system = 1.53891e-09 + Linear momentum = (1.86054e-11 -1.00129e-08 0) + |Linear momentum| = 1.00129e-08 + Linear kinetic energy = 3.39822e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 391.659, 540.2 + Mass transfer phase change = 1.67235e-10 + D10, D32, Dmax (mu) = 63.786, 89.2068, 166.187 + Liquid penetration 95% mass (m) = 0.0106599 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0323441, Final residual = 1.32498e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0987728, Final residual = 2.36115e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00159609, Final residual = 9.10017e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000702446, Final residual = 4.68601e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000674912, Final residual = 5.09723e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00067511, Final residual = 5.11269e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00145517, Final residual = 8.35057e-08, No Iterations 1 +min/max(T) = 770.889, 2796.71 +GAMG: Solving for p, Initial residual = 0.0126066, Final residual = 0.000180243, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.36652e-05, global = 1.24245e-05, cumulative = 0.0037853 +GAMG: Solving for p, Initial residual = 0.000178148, Final residual = 5.54146e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.25493e-05, global = 1.25458e-05, cumulative = 0.00379784 +smoothSolver: Solving for epsilon, Initial residual = 0.000665225, Final residual = 7.44217e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0009142, Final residual = 1.25236e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.107374 s +other Time = 1e-06 s +rho Equations = 0.000174 s +U Equations = 0.001299 s +Y Equations = 0.00245994 s +E Equations = 0.000599 s +p Equations = 0.002264 s +calculate parcels = 114.407 s +chemistry correctThermo = 0.002848 s +turbulence correct = 0.000992 s +combustion correct(in Y) = 0.0965341 s +percentage of chemistry = 89.9045 % +percentage of rho/U/Y/E = 4.22071 % +========Time details of each equation======= +rhoEqn Time = 0.000318 s +rhoEqn assamble = 0.000253 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001298 s +UEqn assamble = 0.000763 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000535 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001817 s +YEqn assamble = 0.000633 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000189 s +YEqn correct boundary = 0 s +EEqn Time = 0.000445 s +EEqn assamble = 0.000327 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 170.36 s ClockTime = 171 s +Courant Number mean: 0.00142199 max: 0.0178198 +Time = 0.0014775 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22385 + Current mass in system = 1.53778e-09 + Linear momentum = (1.86251e-11 -9.99362e-09 0) + |Linear momentum| = 9.99363e-09 + Linear kinetic energy = 3.38771e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 391.814, 540.2 + Mass transfer phase change = 1.68364e-10 + D10, D32, Dmax (mu) = 63.8104, 89.2485, 166.809 + Liquid penetration 95% mass (m) = 0.010678 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0392543, Final residual = 1.50748e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0961927, Final residual = 2.31816e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00164551, Final residual = 9.59983e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000689298, Final residual = 4.63869e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000664149, Final residual = 5.06579e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000664347, Final residual = 5.08138e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00145474, Final residual = 8.28947e-08, No Iterations 1 +min/max(T) = 773.698, 2795.38 +GAMG: Solving for p, Initial residual = 0.0135656, Final residual = 0.000149041, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.3682e-05, global = 1.28928e-05, cumulative = 0.00381073 +GAMG: Solving for p, Initial residual = 0.000147178, Final residual = 4.97087e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.30085e-05, global = 1.30064e-05, cumulative = 0.00382374 +smoothSolver: Solving for epsilon, Initial residual = 0.000661732, Final residual = 7.4078e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000909079, Final residual = 1.24143e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100612 s +other Time = 0 s +rho Equations = 0.000184 s +U Equations = 0.001258 s +Y Equations = 0.00253302 s +E Equations = 0.000624 s +p Equations = 0.002438 s +calculate parcels = 114.785 s +chemistry correctThermo = 0.002897 s +turbulence correct = 0.001071 s +combustion correct(in Y) = 0.089393 s +percentage of chemistry = 88.8492 % +percentage of rho/U/Y/E = 4.57104 % +========Time details of each equation======= +rhoEqn Time = 0.00034 s +rhoEqn assamble = 0.000271 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001257 s +UEqn assamble = 0.000759 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000498 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001891 s +YEqn assamble = 0.000653 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000194 s +YEqn correct boundary = 0 s +EEqn Time = 0.000462 s +EEqn assamble = 0.000347 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 170.84 s ClockTime = 171 s +Courant Number mean: 0.00148931 max: 0.0183706 +Time = 0.00148 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22382 + Current mass in system = 1.53662e-09 + Linear momentum = (1.87053e-11 -9.97412e-09 0) + |Linear momentum| = 9.97414e-09 + Linear kinetic energy = 3.37712e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 391.969, 540.2 + Mass transfer phase change = 1.69523e-10 + D10, D32, Dmax (mu) = 63.9351, 89.2949, 167.451 + Liquid penetration 95% mass (m) = 0.0106951 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0465836, Final residual = 1.76868e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0928034, Final residual = 2.25551e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00165563, Final residual = 9.74943e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000674498, Final residual = 4.56989e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000640708, Final residual = 4.84863e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00064093, Final residual = 4.86339e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00145358, Final residual = 8.16427e-08, No Iterations 1 +min/max(T) = 776.549, 2795.19 +GAMG: Solving for p, Initial residual = 0.0143971, Final residual = 0.000205536, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.44111e-05, global = 1.32243e-05, cumulative = 0.00383696 +GAMG: Solving for p, Initial residual = 0.000204385, Final residual = 4.94713e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.33564e-05, global = 1.33539e-05, cumulative = 0.00385032 +smoothSolver: Solving for epsilon, Initial residual = 0.000668919, Final residual = 7.37212e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000914479, Final residual = 1.24624e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.077543 s +other Time = 1e-06 s +rho Equations = 0.000157 s +U Equations = 0.001016 s +Y Equations = 0.00236414 s +E Equations = 0.00068 s +p Equations = 0.001909 s +calculate parcels = 115.057 s +chemistry correctThermo = 0.002068 s +turbulence correct = 0.000853 s +combustion correct(in Y) = 0.0682649 s +percentage of chemistry = 88.0348 % +percentage of rho/U/Y/E = 5.43845 % +========Time details of each equation======= +rhoEqn Time = 0.000278 s +rhoEqn assamble = 0.00022 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001014 s +UEqn assamble = 0.000577 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000437 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001797 s +YEqn assamble = 0.000636 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000205 s +YEqn correct boundary = 0 s +EEqn Time = 0.000525 s +EEqn assamble = 0.000391 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000134 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 171.19 s ClockTime = 172 s +Courant Number mean: 0.0015597 max: 0.0184866 +Time = 0.0014825 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22379 + Current mass in system = 1.53538e-09 + Linear momentum = (1.86898e-11 -9.95427e-09 0) + |Linear momentum| = 9.95429e-09 + Linear kinetic energy = 3.36642e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 392.113, 540.2 + Mass transfer phase change = 1.70762e-10 + D10, D32, Dmax (mu) = 63.9898, 89.345, 168.108 + Liquid penetration 95% mass (m) = 0.0107129 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0531762, Final residual = 1.86871e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0891656, Final residual = 2.18234e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00181652, Final residual = 1.18198e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000659215, Final residual = 4.39409e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000637606, Final residual = 4.74288e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000637765, Final residual = 4.75786e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00148192, Final residual = 8.35529e-08, No Iterations 1 +min/max(T) = 779.472, 2796.26 +GAMG: Solving for p, Initial residual = 0.0156048, Final residual = 0.000458321, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.59225e-05, global = 1.37265e-05, cumulative = 0.00386405 +GAMG: Solving for p, Initial residual = 0.000454719, Final residual = 4.2966e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.42876e-05, global = 1.42858e-05, cumulative = 0.00387833 +smoothSolver: Solving for epsilon, Initial residual = 0.000702754, Final residual = 7.87472e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000933666, Final residual = 1.29e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102024 s +other Time = 0 s +rho Equations = 0.000182 s +U Equations = 0.001273 s +Y Equations = 0.00206103 s +E Equations = 0.000488 s +p Equations = 0.001994 s +calculate parcels = 115.4 s +chemistry correctThermo = 0.002074 s +turbulence correct = 0.000878 s +combustion correct(in Y) = 0.092873 s +percentage of chemistry = 91.0305 % +percentage of rho/U/Y/E = 3.92459 % +========Time details of each equation======= +rhoEqn Time = 0.000305 s +rhoEqn assamble = 0.000243 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001273 s +UEqn assamble = 0.000773 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.0005 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001414 s +YEqn assamble = 0.00051 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.6e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000369 s +EEqn assamble = 0.000273 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 171.64 s ClockTime = 172 s +Courant Number mean: 0.00164205 max: 0.0184161 +Time = 0.001485 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22373 + Current mass in system = 1.53412e-09 + Linear momentum = (1.9233e-11 -9.93404e-09 0) + |Linear momentum| = 9.93406e-09 + Linear kinetic energy = 3.35555e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 392.276, 540.2 + Mass transfer phase change = 1.72025e-10 + D10, D32, Dmax (mu) = 64.3422, 89.3957, 168.771 + Liquid penetration 95% mass (m) = 0.0107303 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0737817, Final residual = 2.8203e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0869803, Final residual = 2.18984e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00179839, Final residual = 1.16964e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000629904, Final residual = 4.41497e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000608261, Final residual = 4.83035e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000608409, Final residual = 4.84603e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0014704, Final residual = 8.23606e-08, No Iterations 1 +min/max(T) = 782.41, 2796.96 +GAMG: Solving for p, Initial residual = 0.0170223, Final residual = 0.000572825, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.73468e-05, global = 1.42115e-05, cumulative = 0.00389254 +GAMG: Solving for p, Initial residual = 0.000564389, Final residual = 7.87715e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.45651e-05, global = 1.45605e-05, cumulative = 0.0039071 +smoothSolver: Solving for epsilon, Initial residual = 0.000717668, Final residual = 8.21124e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000949868, Final residual = 1.33664e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100221 s +other Time = 0 s +rho Equations = 0.000181 s +U Equations = 0.001282 s +Y Equations = 0.0025866 s +E Equations = 0.000639 s +p Equations = 0.002423 s +calculate parcels = 115.758 s +chemistry correctThermo = 0.002859 s +turbulence correct = 0.001 s +combustion correct(in Y) = 0.0890464 s +percentage of chemistry = 88.85 % +percentage of rho/U/Y/E = 4.67826 % +========Time details of each equation======= +rhoEqn Time = 0.000337 s +rhoEqn assamble = 0.000255 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001281 s +UEqn assamble = 0.000776 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000505 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001929 s +YEqn assamble = 0.000701 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00019 s +YEqn correct boundary = 0 s +EEqn Time = 0.000457 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00012 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 172.09 s ClockTime = 173 s +Courant Number mean: 0.00172546 max: 0.0190426 +Time = 0.0014875 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22372 + Current mass in system = 1.53295e-09 + Linear momentum = (1.93865e-11 -9.91373e-09 0) + |Linear momentum| = 9.91375e-09 + Linear kinetic energy = 3.34454e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 392.437, 540.2 + Mass transfer phase change = 1.73192e-10 + D10, D32, Dmax (mu) = 64.2839, 89.4287, 169.427 + Liquid penetration 95% mass (m) = 0.010747 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0824879, Final residual = 3.23085e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0837929, Final residual = 2.14914e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00160298, Final residual = 9.26613e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000598879, Final residual = 4.18474e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000581368, Final residual = 4.53465e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000581542, Final residual = 4.54863e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.001424, Final residual = 7.77974e-08, No Iterations 1 +min/max(T) = 785.379, 2795.93 +GAMG: Solving for p, Initial residual = 0.0173317, Final residual = 0.000609814, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.66351e-05, global = 1.32241e-05, cumulative = 0.00392033 +GAMG: Solving for p, Initial residual = 0.000605787, Final residual = 3.39481e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.34499e-05, global = 1.34486e-05, cumulative = 0.00393378 +smoothSolver: Solving for epsilon, Initial residual = 0.000709781, Final residual = 7.75052e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000950002, Final residual = 1.30379e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.104874 s +other Time = 1e-06 s +rho Equations = 0.000197 s +U Equations = 0.001309 s +Y Equations = 0.00266139 s +E Equations = 0.000673 s +p Equations = 0.002659 s +calculate parcels = 116.109 s +chemistry correctThermo = 0.003062 s +turbulence correct = 0.001109 s +combustion correct(in Y) = 0.0929986 s +percentage of chemistry = 88.6765 % +percentage of rho/U/Y/E = 4.61543 % +========Time details of each equation======= +rhoEqn Time = 0.000349 s +rhoEqn assamble = 0.000276 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001308 s +UEqn assamble = 0.000782 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000526 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002016 s +YEqn assamble = 0.000722 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00023 s +YEqn correct boundary = 0 s +EEqn Time = 0.000504 s +EEqn assamble = 0.000369 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000135 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 172.55 s ClockTime = 173 s +Courant Number mean: 0.00181113 max: 0.0192799 +Time = 0.00149 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22365 + Current mass in system = 1.53166e-09 + Linear momentum = (1.93494e-11 -9.89299e-09 0) + |Linear momentum| = 9.89301e-09 + Linear kinetic energy = 3.33346e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 392.602, 540.2 + Mass transfer phase change = 1.74482e-10 + D10, D32, Dmax (mu) = 64.4501, 89.4879, 170.082 + Liquid penetration 95% mass (m) = 0.0107644 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0850932, Final residual = 3.16388e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0796253, Final residual = 2.04098e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00176702, Final residual = 1.06056e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000591323, Final residual = 4.11293e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000576652, Final residual = 4.47151e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000576852, Final residual = 4.48499e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00140585, Final residual = 7.37687e-08, No Iterations 1 +min/max(T) = 788.543, 2796.19 +GAMG: Solving for p, Initial residual = 0.0181084, Final residual = 0.000592196, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.73948e-05, global = 1.45318e-05, cumulative = 0.00394831 +GAMG: Solving for p, Initial residual = 0.000582632, Final residual = 5.38354e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.48652e-05, global = 1.48637e-05, cumulative = 0.00396317 +smoothSolver: Solving for epsilon, Initial residual = 0.000695848, Final residual = 7.46073e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000939535, Final residual = 1.26851e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.084941 s +other Time = 0 s +rho Equations = 0.00015 s +U Equations = 0.001104 s +Y Equations = 0.00211314 s +E Equations = 0.0005 s +p Equations = 0.002045 s +calculate parcels = 116.447 s +chemistry correctThermo = 0.002094 s +turbulence correct = 0.000857 s +combustion correct(in Y) = 0.0759039 s +percentage of chemistry = 89.3607 % +percentage of rho/U/Y/E = 4.55274 % +========Time details of each equation======= +rhoEqn Time = 0.000275 s +rhoEqn assamble = 0.000217 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001103 s +UEqn assamble = 0.000677 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000426 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001563 s +YEqn assamble = 0.000548 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000168 s +YEqn correct boundary = 0 s +EEqn Time = 0.000378 s +EEqn assamble = 0.00028 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 172.97 s ClockTime = 173 s +Courant Number mean: 0.0019232 max: 0.0202565 +Time = 0.0014925 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22362 + Current mass in system = 1.53043e-09 + Linear momentum = (1.92759e-11 -9.87278e-09 0) + |Linear momentum| = 9.8728e-09 + Linear kinetic energy = 3.32257e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 392.723, 540.2 + Mass transfer phase change = 1.75715e-10 + D10, D32, Dmax (mu) = 64.4385, 89.5333, 170.735 + Liquid penetration 95% mass (m) = 0.0107803 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0900251, Final residual = 3.11105e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0766225, Final residual = 1.99841e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00166402, Final residual = 9.15694e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000591317, Final residual = 4.07994e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000569672, Final residual = 4.45366e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000569833, Final residual = 4.46771e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00139509, Final residual = 7.40862e-08, No Iterations 1 +min/max(T) = 791.905, 2797.14 +GAMG: Solving for p, Initial residual = 0.0188715, Final residual = 0.000606695, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.73133e-05, global = 1.4144e-05, cumulative = 0.00397732 +GAMG: Solving for p, Initial residual = 0.000587937, Final residual = 3.73367e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.42124e-05, global = 1.42104e-05, cumulative = 0.00399153 +smoothSolver: Solving for epsilon, Initial residual = 0.000703384, Final residual = 7.61003e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000943684, Final residual = 1.29104e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.077091 s +other Time = 1e-06 s +rho Equations = 0.000174 s +U Equations = 0.001189 s +Y Equations = 0.00220373 s +E Equations = 0.00051 s +p Equations = 0.002019 s +calculate parcels = 116.792 s +chemistry correctThermo = 0.002062 s +turbulence correct = 0.000797 s +combustion correct(in Y) = 0.0679323 s +percentage of chemistry = 88.1196 % +percentage of rho/U/Y/E = 5.28821 % +========Time details of each equation======= +rhoEqn Time = 0.000293 s +rhoEqn assamble = 0.000232 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001188 s +UEqn assamble = 0.000747 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000441 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001663 s +YEqn assamble = 0.000557 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000129 s +YEqn correct boundary = 0 s +EEqn Time = 0.000382 s +EEqn assamble = 0.000287 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 173.39 s ClockTime = 174 s +Courant Number mean: 0.00204236 max: 0.020522 +Time = 0.001495 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22359 + Current mass in system = 1.5292e-09 + Linear momentum = (1.92438e-11 -9.85285e-09 0) + |Linear momentum| = 9.85287e-09 + Linear kinetic energy = 3.31184e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 392.843, 540.2 + Mass transfer phase change = 1.76941e-10 + D10, D32, Dmax (mu) = 64.4734, 89.5813, 171.37 + Liquid penetration 95% mass (m) = 0.0107967 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0697624, Final residual = 1.83429e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.07175, Final residual = 1.89525e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00165879, Final residual = 9.16817e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000581559, Final residual = 4.07662e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000554629, Final residual = 4.31022e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00055475, Final residual = 4.32409e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00140492, Final residual = 7.44703e-08, No Iterations 1 +min/max(T) = 795.351, 2797.92 +GAMG: Solving for p, Initial residual = 0.0194831, Final residual = 0.000573226, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.67751e-05, global = 1.42049e-05, cumulative = 0.00400573 +GAMG: Solving for p, Initial residual = 0.000563603, Final residual = 2.78725e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.41365e-05, global = 1.41352e-05, cumulative = 0.00401987 +smoothSolver: Solving for epsilon, Initial residual = 0.000729233, Final residual = 8.00952e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000959086, Final residual = 1.336e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095569 s +other Time = 1e-06 s +rho Equations = 0.000155 s +U Equations = 0.000975 s +Y Equations = 0.00246002 s +E Equations = 0.000592 s +p Equations = 0.002508 s +calculate parcels = 117.061 s +chemistry correctThermo = 0.002903 s +turbulence correct = 0.000994 s +combustion correct(in Y) = 0.084796 s +percentage of chemistry = 88.7275 % +percentage of rho/U/Y/E = 4.37591 % +========Time details of each equation======= +rhoEqn Time = 0.000304 s +rhoEqn assamble = 0.00024 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000974 s +UEqn assamble = 0.000565 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000409 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00187 s +YEqn assamble = 0.000656 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000209 s +YEqn correct boundary = 0 s +EEqn Time = 0.000436 s +EEqn assamble = 0.000324 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 173.76 s ClockTime = 174 s +Courant Number mean: 0.00216535 max: 0.0203048 +Time = 0.0014975 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22356 + Current mass in system = 1.5279e-09 + Linear momentum = (1.91544e-11 -9.83279e-09 0) + |Linear momentum| = 9.83281e-09 + Linear kinetic energy = 3.30113e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 393.018, 540.2 + Mass transfer phase change = 1.78238e-10 + D10, D32, Dmax (mu) = 64.5089, 89.6305, 171.973 + Liquid penetration 95% mass (m) = 0.0108148 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0603098, Final residual = 1.74032e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0678777, Final residual = 1.81921e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00177738, Final residual = 1.05482e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000567819, Final residual = 3.96083e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000550227, Final residual = 4.33245e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000550368, Final residual = 4.34685e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00142072, Final residual = 7.25274e-08, No Iterations 1 +min/max(T) = 798.727, 2798.03 +GAMG: Solving for p, Initial residual = 0.0212349, Final residual = 0.000793424, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.78478e-05, global = 1.4669e-05, cumulative = 0.00403453 +GAMG: Solving for p, Initial residual = 0.000779637, Final residual = 4.88842e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.49531e-05, global = 1.49515e-05, cumulative = 0.00404949 +smoothSolver: Solving for epsilon, Initial residual = 0.000760332, Final residual = 8.62337e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000976725, Final residual = 1.39305e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.105684 s +other Time = 1e-06 s +rho Equations = 0.00023 s +U Equations = 0.001546 s +Y Equations = 0.00260644 s +E Equations = 0.000583 s +p Equations = 0.004053 s +calculate parcels = 117.393 s +chemistry correctThermo = 0.004562 s +turbulence correct = 0.001619 s +combustion correct(in Y) = 0.0902176 s +percentage of chemistry = 85.3654 % +percentage of rho/U/Y/E = 4.69838 % +========Time details of each equation======= +rhoEqn Time = 0.000564 s +rhoEqn assamble = 0.000376 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000188 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001544 s +UEqn assamble = 0.000969 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000575 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001942 s +YEqn assamble = 0.000663 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000248 s +YEqn correct boundary = 0 s +EEqn Time = 0.000426 s +EEqn assamble = 0.000316 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00011 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 174.2 s ClockTime = 175 s +Courant Number mean: 0.00229209 max: 0.0218019 +Time = 0.0015 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22355 + Current mass in system = 1.52671e-09 + Linear momentum = (1.95571e-11 -9.81241e-09 0) + |Linear momentum| = 9.81243e-09 + Linear kinetic energy = 3.29016e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 393.227, 540.2 + Mass transfer phase change = 1.79429e-10 + D10, D32, Dmax (mu) = 64.4783, 89.6632, 171.945 + Liquid penetration 95% mass (m) = 0.0108318 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0731995, Final residual = 2.67085e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0653715, Final residual = 1.80615e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00156463, Final residual = 8.29852e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000540597, Final residual = 4.06027e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000515778, Final residual = 4.25216e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000515987, Final residual = 4.26537e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00138621, Final residual = 7.41937e-08, No Iterations 1 +min/max(T) = 802.031, 2797.56 +GAMG: Solving for p, Initial residual = 0.0227813, Final residual = 0.000986201, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.76952e-05, global = 1.37095e-05, cumulative = 0.0040632 +GAMG: Solving for p, Initial residual = 0.000971719, Final residual = 7.27088e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.37257e-05, global = 1.37227e-05, cumulative = 0.00407692 +smoothSolver: Solving for epsilon, Initial residual = 0.000755434, Final residual = 8.66024e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000977448, Final residual = 1.41804e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.084855 s +other Time = 1e-06 s +rho Equations = 0.000146 s +U Equations = 0.000966 s +Y Equations = 0.00216439 s +E Equations = 0.000481 s +p Equations = 0.001938 s +calculate parcels = 117.75 s +chemistry correctThermo = 0.0021 s +turbulence correct = 0.00082 s +combustion correct(in Y) = 0.0760676 s +percentage of chemistry = 89.6442 % +percentage of rho/U/Y/E = 4.42801 % +========Time details of each equation======= +rhoEqn Time = 0.000266 s +rhoEqn assamble = 0.000207 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000965 s +UEqn assamble = 0.000557 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000408 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00142 s +YEqn assamble = 0.000541 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 4.1e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000365 s +EEqn assamble = 0.000272 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 174.98 s ClockTime = 176 s +Courant Number mean: 0.00240149 max: 0.0204214 +Time = 0.0015025 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22355 + Current mass in system = 1.52553e-09 + Linear momentum = (1.99386e-11 -9.79187e-09 0) + |Linear momentum| = 9.79189e-09 + Linear kinetic energy = 3.27904e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 393.449, 540.2 + Mass transfer phase change = 1.80609e-10 + D10, D32, Dmax (mu) = 64.4007, 89.6927, 171.676 + Liquid penetration 95% mass (m) = 0.0108491 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0670537, Final residual = 2.10896e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0607133, Final residual = 1.69856e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0015054, Final residual = 7.63348e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000530163, Final residual = 3.92697e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000509676, Final residual = 4.18221e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000509903, Final residual = 4.19505e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00136493, Final residual = 7.22147e-08, No Iterations 1 +min/max(T) = 805.516, 2796.99 +GAMG: Solving for p, Initial residual = 0.0232207, Final residual = 0.00059128, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.62374e-05, global = 1.35088e-05, cumulative = 0.00409043 +GAMG: Solving for p, Initial residual = 0.00058445, Final residual = 3.45721e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.3606e-05, global = 1.36048e-05, cumulative = 0.00410403 +smoothSolver: Solving for epsilon, Initial residual = 0.000748349, Final residual = 8.49981e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000973079, Final residual = 1.41452e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103521 s +other Time = 0 s +rho Equations = 0.000202 s +U Equations = 0.001183 s +Y Equations = 0.00244592 s +E Equations = 0.000593 s +p Equations = 0.002439 s +calculate parcels = 118.101 s +chemistry correctThermo = 0.00284 s +turbulence correct = 0.001164 s +combustion correct(in Y) = 0.0924521 s +percentage of chemistry = 89.3076 % +percentage of rho/U/Y/E = 4.27345 % +========Time details of each equation======= +rhoEqn Time = 0.000343 s +rhoEqn assamble = 0.000271 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001182 s +UEqn assamble = 0.00068 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000502 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001809 s +YEqn assamble = 0.000648 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000193 s +YEqn correct boundary = 0 s +EEqn Time = 0.000439 s +EEqn assamble = 0.000326 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 175.44 s ClockTime = 176 s +Courant Number mean: 0.00251062 max: 0.0206938 +Time = 0.001505 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22355 + Current mass in system = 1.52436e-09 + Linear momentum = (2.01884e-11 -9.77162e-09 0) + |Linear momentum| = 9.77164e-09 + Linear kinetic energy = 3.26807e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 393.673, 540.2 + Mass transfer phase change = 1.81786e-10 + D10, D32, Dmax (mu) = 64.3327, 89.7243, 172.03 + Liquid penetration 95% mass (m) = 0.0108657 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.070493, Final residual = 1.91482e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0565102, Final residual = 1.60338e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00148464, Final residual = 7.30453e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000528743, Final residual = 3.87757e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000511907, Final residual = 4.15056e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000512131, Final residual = 4.16343e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.001356, Final residual = 7.02354e-08, No Iterations 1 +min/max(T) = 805.866, 2796.81 +GAMG: Solving for p, Initial residual = 0.0244814, Final residual = 0.000522571, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.57671e-05, global = 1.34619e-05, cumulative = 0.00411749 +GAMG: Solving for p, Initial residual = 0.000512394, Final residual = 2.64547e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.35667e-05, global = 1.35659e-05, cumulative = 0.00413106 +smoothSolver: Solving for epsilon, Initial residual = 0.000748224, Final residual = 8.44895e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000972739, Final residual = 1.41243e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.075967 s +other Time = 1e-06 s +rho Equations = 0.000213 s +U Equations = 0.001021 s +Y Equations = 0.00257887 s +E Equations = 0.000496 s +p Equations = 0.002188 s +calculate parcels = 118.431 s +chemistry correctThermo = 0.001991 s +turbulence correct = 0.000906 s +combustion correct(in Y) = 0.0662761 s +percentage of chemistry = 87.2433 % +percentage of rho/U/Y/E = 5.67202 % +========Time details of each equation======= +rhoEqn Time = 0.000335 s +rhoEqn assamble = 0.00027 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00102 s +UEqn assamble = 0.00061 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00041 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002003 s +YEqn assamble = 0.000668 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00016 s +YEqn correct boundary = 0 s +EEqn Time = 0.000368 s +EEqn assamble = 0.000275 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 175.85 s ClockTime = 176 s +Courant Number mean: 0.00262297 max: 0.0209372 +Time = 0.0015075 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22354 + Current mass in system = 1.52316e-09 + Linear momentum = (2.0285e-11 -9.75173e-09 0) + |Linear momentum| = 9.75175e-09 + Linear kinetic energy = 3.25738e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 393.901, 540.2 + Mass transfer phase change = 1.82984e-10 + D10, D32, Dmax (mu) = 64.316, 89.7636, 172.662 + Liquid penetration 95% mass (m) = 0.0108826 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0675264, Final residual = 1.69152e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.052282, Final residual = 1.50312e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00147527, Final residual = 7.26515e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000527682, Final residual = 3.90976e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000514303, Final residual = 4.1355e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000514511, Final residual = 4.14811e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00134686, Final residual = 7.01068e-08, No Iterations 1 +min/max(T) = 805.905, 2797.02 +GAMG: Solving for p, Initial residual = 0.0261485, Final residual = 0.00051868, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.58083e-05, global = 1.3713e-05, cumulative = 0.00414477 +GAMG: Solving for p, Initial residual = 0.000513347, Final residual = 3.6529e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.38034e-05, global = 1.38024e-05, cumulative = 0.00415858 +smoothSolver: Solving for epsilon, Initial residual = 0.000753337, Final residual = 8.50868e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00097339, Final residual = 1.41637e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.106269 s +other Time = 0 s +rho Equations = 0.00018 s +U Equations = 0.00123 s +Y Equations = 0.00221894 s +E Equations = 0.000497 s +p Equations = 0.002056 s +calculate parcels = 118.741 s +chemistry correctThermo = 0.002052 s +turbulence correct = 0.001181 s +combustion correct(in Y) = 0.0966471 s +percentage of chemistry = 90.9457 % +percentage of rho/U/Y/E = 3.88255 % +========Time details of each equation======= +rhoEqn Time = 0.000337 s +rhoEqn assamble = 0.000268 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001229 s +UEqn assamble = 0.000716 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000513 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001486 s +YEqn assamble = 0.000558 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 6.8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000375 s +EEqn assamble = 0.000278 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.7e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 176.26 s ClockTime = 177 s +Courant Number mean: 0.00273228 max: 0.0189029 +Time = 0.00151 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22354 + Current mass in system = 1.52198e-09 + Linear momentum = (2.02322e-11 -9.73215e-09 0) + |Linear momentum| = 9.73217e-09 + Linear kinetic energy = 3.24686e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 394.148, 540.2 + Mass transfer phase change = 1.84161e-10 + D10, D32, Dmax (mu) = 64.2469, 89.7954, 173.31 + Liquid penetration 95% mass (m) = 0.0108993 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0623351, Final residual = 1.68946e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0478192, Final residual = 1.39929e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00148416, Final residual = 7.37271e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00052138, Final residual = 3.8507e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000519642, Final residual = 4.10445e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000519819, Final residual = 4.11709e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00135051, Final residual = 7.038e-08, No Iterations 1 +min/max(T) = 805.963, 2797.36 +GAMG: Solving for p, Initial residual = 0.0282596, Final residual = 0.000532542, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.55158e-05, global = 1.35615e-05, cumulative = 0.00417214 +GAMG: Solving for p, Initial residual = 0.000528412, Final residual = 2.93275e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.35692e-05, global = 1.35681e-05, cumulative = 0.0041857 +smoothSolver: Solving for epsilon, Initial residual = 0.000756277, Final residual = 8.61917e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0009675, Final residual = 1.42283e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.106508 s +other Time = 1e-06 s +rho Equations = 0.000184 s +U Equations = 0.001168 s +Y Equations = 0.00208941 s +E Equations = 0.000473 s +p Equations = 0.002614 s +calculate parcels = 119.104 s +chemistry correctThermo = 0.00251 s +turbulence correct = 0.001068 s +combustion correct(in Y) = 0.0962026 s +percentage of chemistry = 90.3243 % +percentage of rho/U/Y/E = 3.67522 % +========Time details of each equation======= +rhoEqn Time = 0.000339 s +rhoEqn assamble = 0.000266 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001168 s +UEqn assamble = 0.000664 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000504 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001458 s +YEqn assamble = 0.000515 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.7e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000357 s +EEqn assamble = 0.000266 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 176.73 s ClockTime = 177 s +Courant Number mean: 0.00284124 max: 0.0203859 +Time = 0.0015125 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22352 + Current mass in system = 1.52079e-09 + Linear momentum = (2.00677e-11 -9.71236e-09 0) + |Linear momentum| = 9.71238e-09 + Linear kinetic energy = 3.23627e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 394.385, 540.2 + Mass transfer phase change = 1.85357e-10 + D10, D32, Dmax (mu) = 64.3634, 89.8291, 173.969 + Liquid penetration 95% mass (m) = 0.0109167 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.048739, Final residual = 1.46162e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0433214, Final residual = 1.29291e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00149053, Final residual = 7.38178e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000515123, Final residual = 3.79996e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000516964, Final residual = 4.03454e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000517154, Final residual = 4.04741e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00135872, Final residual = 7.03625e-08, No Iterations 1 +min/max(T) = 806.032, 2797.55 +GAMG: Solving for p, Initial residual = 0.0306297, Final residual = 0.000537087, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.55172e-05, global = 1.36532e-05, cumulative = 0.00419936 +GAMG: Solving for p, Initial residual = 0.000536007, Final residual = 1.83194e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.37859e-05, global = 1.37853e-05, cumulative = 0.00421314 +smoothSolver: Solving for epsilon, Initial residual = 0.000764239, Final residual = 8.82013e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00096773, Final residual = 1.44343e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.106915 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001214 s +Y Equations = 0.00242946 s +E Equations = 0.000597 s +p Equations = 0.002505 s +calculate parcels = 119.462 s +chemistry correctThermo = 0.002903 s +turbulence correct = 0.001067 s +combustion correct(in Y) = 0.0958185 s +percentage of chemistry = 89.6212 % +percentage of rho/U/Y/E = 4.13175 % +========Time details of each equation======= +rhoEqn Time = 0.000325 s +rhoEqn assamble = 0.000256 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001212 s +UEqn assamble = 0.000689 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000523 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001784 s +YEqn assamble = 0.000627 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000199 s +YEqn correct boundary = 0 s +EEqn Time = 0.000442 s +EEqn assamble = 0.00033 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 177.2 s ClockTime = 178 s +Courant Number mean: 0.00293903 max: 0.0198347 +Time = 0.001515 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22350 + Current mass in system = 1.51954e-09 + Linear momentum = (1.98875e-11 -9.69189e-09 0) + |Linear momentum| = 9.69191e-09 + Linear kinetic energy = 3.22534e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 394.619, 540.2 + Mass transfer phase change = 1.86602e-10 + D10, D32, Dmax (mu) = 64.4061, 89.8646, 174.631 + Liquid penetration 95% mass (m) = 0.0109339 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0426542, Final residual = 1.25138e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0396436, Final residual = 1.207e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00153715, Final residual = 8.08114e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000515114, Final residual = 3.78623e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000521148, Final residual = 4.07336e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000521348, Final residual = 4.08674e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00137268, Final residual = 6.97076e-08, No Iterations 1 +min/max(T) = 806.106, 2797.45 +GAMG: Solving for p, Initial residual = 0.0328757, Final residual = 0.000590851, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.61053e-05, global = 1.41441e-05, cumulative = 0.00422729 +GAMG: Solving for p, Initial residual = 0.000590503, Final residual = 2.32631e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.4354e-05, global = 1.43532e-05, cumulative = 0.00424164 +smoothSolver: Solving for epsilon, Initial residual = 0.000775533, Final residual = 9.1549e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000969349, Final residual = 1.47593e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.090581 s +other Time = 1e-06 s +rho Equations = 0.000209 s +U Equations = 0.00125 s +Y Equations = 0.00247807 s +E Equations = 0.000525 s +p Equations = 0.001905 s +calculate parcels = 119.823 s +chemistry correctThermo = 0.002029 s +turbulence correct = 0.000837 s +combustion correct(in Y) = 0.0811409 s +percentage of chemistry = 89.5783 % +percentage of rho/U/Y/E = 4.92606 % +========Time details of each equation======= +rhoEqn Time = 0.000323 s +rhoEqn assamble = 0.000253 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001249 s +UEqn assamble = 0.000758 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000491 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001851 s +YEqn assamble = 0.000638 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000169 s +YEqn correct boundary = 0 s +EEqn Time = 0.000399 s +EEqn assamble = 0.000302 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.7e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 177.65 s ClockTime = 178 s +Courant Number mean: 0.0030277 max: 0.0186499 +Time = 0.0015175 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22348 + Current mass in system = 1.5182e-09 + Linear momentum = (1.96132e-11 -9.67036e-09 0) + |Linear momentum| = 9.67038e-09 + Linear kinetic energy = 3.21389e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 394.866, 540.2 + Mass transfer phase change = 1.87944e-10 + D10, D32, Dmax (mu) = 64.3532, 89.8977, 175.292 + Liquid penetration 95% mass (m) = 0.010951 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0465807, Final residual = 1.26838e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0363095, Final residual = 1.12987e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00165709, Final residual = 9.32179e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000505196, Final residual = 3.6748e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000524191, Final residual = 4.06718e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000524351, Final residual = 4.08107e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00139324, Final residual = 6.99269e-08, No Iterations 1 +min/max(T) = 806.184, 2796.66 +GAMG: Solving for p, Initial residual = 0.0361603, Final residual = 0.000851853, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.79433e-05, global = 1.50247e-05, cumulative = 0.00425667 +GAMG: Solving for p, Initial residual = 0.000861391, Final residual = 5.95835e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.54615e-05, global = 1.54594e-05, cumulative = 0.00427212 +smoothSolver: Solving for epsilon, Initial residual = 0.000803053, Final residual = 9.90854e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000985695, Final residual = 1.5458e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09423 s +other Time = 1e-06 s +rho Equations = 0.00015 s +U Equations = 0.001036 s +Y Equations = 0.00239151 s +E Equations = 0.00051 s +p Equations = 0.002071 s +calculate parcels = 120.18 s +chemistry correctThermo = 0.002011 s +turbulence correct = 0.000861 s +combustion correct(in Y) = 0.0849725 s +percentage of chemistry = 90.1756 % +percentage of rho/U/Y/E = 4.3378 % +========Time details of each equation======= +rhoEqn Time = 0.000273 s +rhoEqn assamble = 0.000213 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001034 s +UEqn assamble = 0.000577 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000457 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001817 s +YEqn assamble = 0.000665 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000161 s +YEqn correct boundary = 0 s +EEqn Time = 0.000382 s +EEqn assamble = 0.000287 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 178.1 s ClockTime = 179 s +Courant Number mean: 0.00310862 max: 0.019778 +Time = 0.00152 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22346 + Current mass in system = 1.51693e-09 + Linear momentum = (1.91899e-11 -9.64791e-09 0) + |Linear momentum| = 9.64793e-09 + Linear kinetic energy = 3.20185e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 395.119, 540.2 + Mass transfer phase change = 1.89216e-10 + D10, D32, Dmax (mu) = 64.423, 89.921, 175.94 + Liquid penetration 95% mass (m) = 0.0109677 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0698639, Final residual = 2.25488e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0332403, Final residual = 1.06451e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00150066, Final residual = 7.4357e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000483216, Final residual = 3.61045e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00049633, Final residual = 3.7844e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000496471, Final residual = 3.79652e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00137065, Final residual = 6.88752e-08, No Iterations 1 +min/max(T) = 806.243, 2794.94 +GAMG: Solving for p, Initial residual = 0.0387936, Final residual = 0.00106923, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.73811e-05, global = 1.46346e-05, cumulative = 0.00428676 +GAMG: Solving for p, Initial residual = 0.00108091, Final residual = 6.04502e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.46616e-05, global = 1.46603e-05, cumulative = 0.00430142 +smoothSolver: Solving for epsilon, Initial residual = 0.000814674, Final residual = 9.84916e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00100094, Final residual = 1.57173e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.085663 s +other Time = 0 s +rho Equations = 0.000179 s +U Equations = 0.001111 s +Y Equations = 0.00213303 s +E Equations = 0.000503 s +p Equations = 0.002557 s +calculate parcels = 120.45 s +chemistry correctThermo = 0.002054 s +turbulence correct = 0.001101 s +combustion correct(in Y) = 0.075823 s +percentage of chemistry = 88.5131 % +percentage of rho/U/Y/E = 4.58311 % +========Time details of each equation======= +rhoEqn Time = 0.000335 s +rhoEqn assamble = 0.000265 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00111 s +UEqn assamble = 0.000665 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000445 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001579 s +YEqn assamble = 0.000552 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000178 s +YEqn correct boundary = 0 s +EEqn Time = 0.000378 s +EEqn assamble = 0.000282 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 178.46 s ClockTime = 179 s +Courant Number mean: 0.00316641 max: 0.0181916 +Time = 0.0015225 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22345 + Current mass in system = 1.51561e-09 + Linear momentum = (1.87734e-11 -9.62464e-09 0) + |Linear momentum| = 9.62466e-09 + Linear kinetic energy = 3.18934e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 395.371, 540.2 + Mass transfer phase change = 1.90531e-10 + D10, D32, Dmax (mu) = 64.3713, 89.9424, 176.57 + Liquid penetration 95% mass (m) = 0.0109838 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0907143, Final residual = 3.01017e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0293579, Final residual = 9.61318e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00152117, Final residual = 7.65242e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00047218, Final residual = 3.47175e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000488899, Final residual = 3.76472e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000489027, Final residual = 3.77667e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00134897, Final residual = 6.51104e-08, No Iterations 1 +min/max(T) = 806.297, 2793.55 +GAMG: Solving for p, Initial residual = 0.0414706, Final residual = 0.000572509, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.67957e-05, global = 1.50727e-05, cumulative = 0.00431649 +GAMG: Solving for p, Initial residual = 0.000571548, Final residual = 2.08829e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.51564e-05, global = 1.51559e-05, cumulative = 0.00433165 +smoothSolver: Solving for epsilon, Initial residual = 0.000821797, Final residual = 1.00737e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00100606, Final residual = 1.59705e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102335 s +other Time = 0 s +rho Equations = 0.0002 s +U Equations = 0.001274 s +Y Equations = 0.00241782 s +E Equations = 0.000604 s +p Equations = 0.002463 s +calculate parcels = 120.796 s +chemistry correctThermo = 0.002853 s +turbulence correct = 0.000962 s +combustion correct(in Y) = 0.0913632 s +percentage of chemistry = 89.2785 % +percentage of rho/U/Y/E = 4.39324 % +========Time details of each equation======= +rhoEqn Time = 0.000342 s +rhoEqn assamble = 0.00026 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001274 s +UEqn assamble = 0.000758 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000516 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00177 s +YEqn assamble = 0.000646 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000179 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 178.9 s ClockTime = 179 s +Courant Number mean: 0.00322648 max: 0.0182021 +Time = 0.001525 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22344 + Current mass in system = 1.5143e-09 + Linear momentum = (1.83108e-11 -9.60086e-09 0) + |Linear momentum| = 9.60087e-09 + Linear kinetic energy = 3.17652e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 395.62, 540.2 + Mass transfer phase change = 1.9184e-10 + D10, D32, Dmax (mu) = 64.3113, 89.9569, 177.175 + Liquid penetration 95% mass (m) = 0.011 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0966393, Final residual = 3.17533e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0266369, Final residual = 8.84409e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00148526, Final residual = 7.20149e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000462468, Final residual = 3.42836e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000481855, Final residual = 3.65669e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000481962, Final residual = 3.66827e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00132602, Final residual = 6.4533e-08, No Iterations 1 +min/max(T) = 806.345, 2792.25 +GAMG: Solving for p, Initial residual = 0.0444256, Final residual = 0.000777122, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.71052e-05, global = 1.51286e-05, cumulative = 0.00434678 +GAMG: Solving for p, Initial residual = 0.00078609, Final residual = 5.63466e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.5097e-05, global = 1.50961e-05, cumulative = 0.00436187 +smoothSolver: Solving for epsilon, Initial residual = 0.00083655, Final residual = 1.02073e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00101772, Final residual = 1.61839e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095455 s +other Time = 0 s +rho Equations = 0.000153 s +U Equations = 0.001063 s +Y Equations = 0.00207564 s +E Equations = 0.000486 s +p Equations = 0.002012 s +calculate parcels = 121.12 s +chemistry correctThermo = 0.002019 s +turbulence correct = 0.001426 s +combustion correct(in Y) = 0.0860334 s +percentage of chemistry = 90.1298 % +percentage of rho/U/Y/E = 3.95751 % +========Time details of each equation======= +rhoEqn Time = 0.000296 s +rhoEqn assamble = 0.000234 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001063 s +UEqn assamble = 0.000648 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000415 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001511 s +YEqn assamble = 0.000531 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00014 s +YEqn correct boundary = 0 s +EEqn Time = 0.000365 s +EEqn assamble = 0.000272 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 179.32 s ClockTime = 180 s +Courant Number mean: 0.0032846 max: 0.0182809 +Time = 0.0015275 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22344 + Current mass in system = 1.513e-09 + Linear momentum = (1.80516e-11 -9.57685e-09 0) + |Linear momentum| = 9.57687e-09 + Linear kinetic energy = 3.16355e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 395.863, 540.2 + Mass transfer phase change = 1.93139e-10 + D10, D32, Dmax (mu) = 64.23, 89.9649, 177.291 + Liquid penetration 95% mass (m) = 0.0110167 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0979186, Final residual = 3.067e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0251818, Final residual = 8.46664e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00145539, Final residual = 6.63007e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000454764, Final residual = 3.4869e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000476411, Final residual = 3.709e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000476517, Final residual = 3.72029e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00131692, Final residual = 6.36455e-08, No Iterations 1 +min/max(T) = 806.384, 2791.15 +GAMG: Solving for p, Initial residual = 0.048253, Final residual = 0.000818551, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.70335e-05, global = 1.51213e-05, cumulative = 0.00437699 +GAMG: Solving for p, Initial residual = 0.000829931, Final residual = 4.00569e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.49723e-05, global = 1.49713e-05, cumulative = 0.00439197 +smoothSolver: Solving for epsilon, Initial residual = 0.00083697, Final residual = 1.03654e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0010165, Final residual = 1.62915e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.104822 s +other Time = 0 s +rho Equations = 0.000184 s +U Equations = 0.001261 s +Y Equations = 0.00245365 s +E Equations = 0.000598 s +p Equations = 0.002928 s +calculate parcels = 121.463 s +chemistry correctThermo = 0.002993 s +turbulence correct = 0.001101 s +combustion correct(in Y) = 0.0930703 s +percentage of chemistry = 88.7889 % +percentage of rho/U/Y/E = 4.2898 % +========Time details of each equation======= +rhoEqn Time = 0.00035 s +rhoEqn assamble = 0.000279 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00126 s +UEqn assamble = 0.000735 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000525 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001788 s +YEqn assamble = 0.000656 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000173 s +YEqn correct boundary = 0 s +EEqn Time = 0.000442 s +EEqn assamble = 0.00033 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 179.77 s ClockTime = 180 s +Courant Number mean: 0.00334373 max: 0.0178084 +Time = 0.00153 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22341 + Current mass in system = 1.5116e-09 + Linear momentum = (1.80427e-11 -9.55227e-09 0) + |Linear momentum| = 9.55228e-09 + Linear kinetic energy = 3.15038e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 396.109, 540.2 + Mass transfer phase change = 1.94548e-10 + D10, D32, Dmax (mu) = 64.2572, 89.9876, 177.01 + Liquid penetration 95% mass (m) = 0.0110342 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0748024, Final residual = 2.29895e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.02324, Final residual = 7.87848e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00160148, Final residual = 9.10309e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000454081, Final residual = 3.48157e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000479068, Final residual = 3.78165e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00047916, Final residual = 3.79351e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00132597, Final residual = 6.58357e-08, No Iterations 1 +min/max(T) = 806.417, 2789.93 +GAMG: Solving for p, Initial residual = 0.0540293, Final residual = 0.00129283, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.86242e-05, global = 1.62792e-05, cumulative = 0.00440824 +GAMG: Solving for p, Initial residual = 0.00131546, Final residual = 2.53113e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.62344e-05, global = 1.62339e-05, cumulative = 0.00442448 +smoothSolver: Solving for epsilon, Initial residual = 0.000853594, Final residual = 1.09196e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00101994, Final residual = 1.66806e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.093476 s +other Time = 0 s +rho Equations = 0.000173 s +U Equations = 0.001092 s +Y Equations = 0.00212464 s +E Equations = 0.000481 s +p Equations = 0.002145 s +calculate parcels = 121.801 s +chemistry correctThermo = 0.002011 s +turbulence correct = 0.000848 s +combustion correct(in Y) = 0.0844174 s +percentage of chemistry = 90.3091 % +percentage of rho/U/Y/E = 4.14078 % +========Time details of each equation======= +rhoEqn Time = 0.000295 s +rhoEqn assamble = 0.00023 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001092 s +UEqn assamble = 0.000663 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000429 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001565 s +YEqn assamble = 0.000526 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000178 s +YEqn correct boundary = 0 s +EEqn Time = 0.000364 s +EEqn assamble = 0.000273 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 180.2 s ClockTime = 181 s +Courant Number mean: 0.00340712 max: 0.0183404 +Time = 0.0015325 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22337 + Current mass in system = 1.51014e-09 + Linear momentum = (1.78561e-11 -9.52685e-09 0) + |Linear momentum| = 9.52686e-09 + Linear kinetic energy = 3.13682e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 396.361, 540.2 + Mass transfer phase change = 1.96005e-10 + D10, D32, Dmax (mu) = 64.4003, 90.0055, 176.729 + Liquid penetration 95% mass (m) = 0.0110513 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0625045, Final residual = 2.24321e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0219499, Final residual = 7.46994e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00166222, Final residual = 9.21066e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000445117, Final residual = 3.41083e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000473174, Final residual = 3.6374e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000473182, Final residual = 3.64931e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00133496, Final residual = 6.59755e-08, No Iterations 1 +min/max(T) = 806.445, 2787.45 +GAMG: Solving for p, Initial residual = 0.0615751, Final residual = 0.00143207, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.94853e-05, global = 1.67681e-05, cumulative = 0.00444125 +GAMG: Solving for p, Initial residual = 0.00146475, Final residual = 9.52532e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.67989e-05, global = 1.6797e-05, cumulative = 0.00445804 +smoothSolver: Solving for epsilon, Initial residual = 0.000885173, Final residual = 1.15512e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00104267, Final residual = 1.72892e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.074674 s +other Time = 1e-06 s +rho Equations = 0.000174 s +U Equations = 0.001129 s +Y Equations = 0.00219359 s +E Equations = 0.000496 s +p Equations = 0.001939 s +calculate parcels = 122.139 s +chemistry correctThermo = 0.001929 s +turbulence correct = 0.000991 s +combustion correct(in Y) = 0.0656254 s +percentage of chemistry = 87.8825 % +percentage of rho/U/Y/E = 5.34669 % +========Time details of each equation======= +rhoEqn Time = 0.000296 s +rhoEqn assamble = 0.000236 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001129 s +UEqn assamble = 0.000684 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000445 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001613 s +YEqn assamble = 0.000554 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000146 s +YEqn correct boundary = 0 s +EEqn Time = 0.000369 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 180.62 s ClockTime = 181 s +Courant Number mean: 0.00346151 max: 0.0236752 +Time = 0.001535 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22336 + Current mass in system = 1.50876e-09 + Linear momentum = (1.744e-11 -9.50063e-09 0) + |Linear momentum| = 9.50065e-09 + Linear kinetic energy = 3.12275e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 396.612, 540.2 + Mass transfer phase change = 1.97385e-10 + D10, D32, Dmax (mu) = 64.3444, 90.0043, 176.45 + Liquid penetration 95% mass (m) = 0.0110678 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.053231, Final residual = 2.09547e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0209257, Final residual = 7.17499e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00149297, Final residual = 7.00636e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000440113, Final residual = 3.36022e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000460814, Final residual = 3.49097e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000460706, Final residual = 3.50192e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00129724, Final residual = 6.06348e-08, No Iterations 1 +min/max(T) = 806.471, 2784.94 +GAMG: Solving for p, Initial residual = 0.0681857, Final residual = 0.00167474, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.85736e-05, global = 1.61861e-05, cumulative = 0.00447423 +GAMG: Solving for p, Initial residual = 0.00176478, Final residual = 3.28172e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.59069e-05, global = 1.59065e-05, cumulative = 0.00449014 +smoothSolver: Solving for epsilon, Initial residual = 0.000891736, Final residual = 1.1573e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00104817, Final residual = 1.7463e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.099497 s +other Time = 0 s +rho Equations = 0.000156 s +U Equations = 0.001061 s +Y Equations = 0.00259238 s +E Equations = 0.000641 s +p Equations = 0.002982 s +calculate parcels = 122.429 s +chemistry correctThermo = 0.002897 s +turbulence correct = 0.001085 s +combustion correct(in Y) = 0.0878716 s +percentage of chemistry = 88.3158 % +percentage of rho/U/Y/E = 4.47288 % +========Time details of each equation======= +rhoEqn Time = 0.000322 s +rhoEqn assamble = 0.000254 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001061 s +UEqn assamble = 0.00065 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000411 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00203 s +YEqn assamble = 0.000687 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000246 s +YEqn correct boundary = 0 s +EEqn Time = 0.000472 s +EEqn assamble = 0.000357 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 181.01 s ClockTime = 182 s +Courant Number mean: 0.00349888 max: 0.0175528 +Time = 0.0015375 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22336 + Current mass in system = 1.50739e-09 + Linear momentum = (1.69653e-11 -9.47377e-09 0) + |Linear momentum| = 9.47379e-09 + Linear kinetic energy = 3.10827e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 396.861, 540.2 + Mass transfer phase change = 1.98756e-10 + D10, D32, Dmax (mu) = 64.2513, 89.9945, 176.17 + Liquid penetration 95% mass (m) = 0.0110854 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.04137, Final residual = 1.54143e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.019133, Final residual = 6.39485e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00144754, Final residual = 6.52913e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000434025, Final residual = 3.34319e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000458199, Final residual = 3.46208e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000458081, Final residual = 3.47264e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00127512, Final residual = 5.95653e-08, No Iterations 1 +min/max(T) = 806.495, 2782.82 +GAMG: Solving for p, Initial residual = 0.0775168, Final residual = 0.00130639, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.79757e-05, global = 1.59645e-05, cumulative = 0.0045061 +GAMG: Solving for p, Initial residual = 0.00138116, Final residual = 9.19149e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.58045e-05, global = 1.58033e-05, cumulative = 0.0045219 +smoothSolver: Solving for epsilon, Initial residual = 0.00088658, Final residual = 1.14581e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00104459, Final residual = 1.73963e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.105089 s +other Time = 0 s +rho Equations = 0.000187 s +U Equations = 0.001353 s +Y Equations = 0.00254131 s +E Equations = 0.000591 s +p Equations = 0.002449 s +calculate parcels = 122.783 s +chemistry correctThermo = 0.002879 s +turbulence correct = 0.001026 s +combustion correct(in Y) = 0.0938577 s +percentage of chemistry = 89.3126 % +percentage of rho/U/Y/E = 4.44605 % +========Time details of each equation======= +rhoEqn Time = 0.000336 s +rhoEqn assamble = 0.000266 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001351 s +UEqn assamble = 0.000788 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000563 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001796 s +YEqn assamble = 0.000642 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000169 s +YEqn correct boundary = 0 s +EEqn Time = 0.000434 s +EEqn assamble = 0.000321 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 181.46 s ClockTime = 182 s +Courant Number mean: 0.00352382 max: 0.0163809 +Time = 0.00154 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22335 + Current mass in system = 1.50597e-09 + Linear momentum = (1.6625e-11 -9.44651e-09 0) + |Linear momentum| = 9.44653e-09 + Linear kinetic energy = 3.09361e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 397.108, 540.2 + Mass transfer phase change = 2.00169e-10 + D10, D32, Dmax (mu) = 64.1829, 89.9883, 175.888 + Liquid penetration 95% mass (m) = 0.0111018 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0374333, Final residual = 1.27704e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0179264, Final residual = 6.03996e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00148515, Final residual = 7.11568e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000438997, Final residual = 3.40966e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000461882, Final residual = 3.55393e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000461766, Final residual = 3.5646e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00127146, Final residual = 5.97869e-08, No Iterations 1 +min/max(T) = 806.527, 2781.65 +GAMG: Solving for p, Initial residual = 0.0926938, Final residual = 0.00165722, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.83161e-05, global = 1.63537e-05, cumulative = 0.00453826 +GAMG: Solving for p, Initial residual = 0.00175394, Final residual = 2.32393e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.62837e-05, global = 1.62835e-05, cumulative = 0.00455454 +smoothSolver: Solving for epsilon, Initial residual = 0.000890937, Final residual = 1.15206e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00104168, Final residual = 1.7374e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.090528 s +other Time = 1e-06 s +rho Equations = 0.000188 s +U Equations = 0.00133 s +Y Equations = 0.00211076 s +E Equations = 0.000479 s +p Equations = 0.002237 s +calculate parcels = 123.145 s +chemistry correctThermo = 0.002016 s +turbulence correct = 0.000804 s +combustion correct(in Y) = 0.0811662 s +percentage of chemistry = 89.6587 % +percentage of rho/U/Y/E = 4.53756 % +========Time details of each equation======= +rhoEqn Time = 0.000313 s +rhoEqn assamble = 0.000245 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001329 s +UEqn assamble = 0.000799 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00053 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001447 s +YEqn assamble = 0.000529 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.5e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000361 s +EEqn assamble = 0.000268 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 181.92 s ClockTime = 182 s +Courant Number mean: 0.00354981 max: 0.0163691 +Time = 0.0015425 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22330 + Current mass in system = 1.50445e-09 + Linear momentum = (1.65914e-11 -9.41849e-09 0) + |Linear momentum| = 9.41851e-09 + Linear kinetic energy = 3.07871e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 397.352, 540.2 + Mass transfer phase change = 2.01691e-10 + D10, D32, Dmax (mu) = 64.2913, 90.0002, 175.6 + Liquid penetration 95% mass (m) = 0.0111175 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0428815, Final residual = 1.44084e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0169874, Final residual = 5.66488e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00162258, Final residual = 8.7438e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000444912, Final residual = 3.57415e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000454761, Final residual = 3.61392e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00045464, Final residual = 3.62433e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00130683, Final residual = 6.13737e-08, No Iterations 1 +min/max(T) = 806.562, 2780.79 +GAMG: Solving for p, Initial residual = 0.115036, Final residual = 0.00262735, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.9694e-05, global = 1.74708e-05, cumulative = 0.00457201 +GAMG: Solving for p, Initial residual = 0.0028269, Final residual = 8.17844e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.75375e-05, global = 1.75367e-05, cumulative = 0.00458955 +smoothSolver: Solving for epsilon, Initial residual = 0.000910536, Final residual = 1.19209e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00104603, Final residual = 1.75569e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.106181 s +other Time = 0 s +rho Equations = 0.000151 s +U Equations = 0.00133 s +Y Equations = 0.00246242 s +E Equations = 0.000607 s +p Equations = 0.002568 s +calculate parcels = 123.469 s +chemistry correctThermo = 0.002839 s +turbulence correct = 0.001016 s +combustion correct(in Y) = 0.0950266 s +percentage of chemistry = 89.4949 % +percentage of rho/U/Y/E = 4.28553 % +========Time details of each equation======= +rhoEqn Time = 0.000294 s +rhoEqn assamble = 0.000232 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001328 s +UEqn assamble = 0.000779 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000549 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001792 s +YEqn assamble = 0.000634 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000191 s +YEqn correct boundary = 0 s +EEqn Time = 0.000447 s +EEqn assamble = 0.000333 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 182.35 s ClockTime = 183 s +Courant Number mean: 0.00358393 max: 0.0168186 +Time = 0.001545 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22329 + Current mass in system = 1.503e-09 + Linear momentum = (1.65396e-11 -9.38986e-09 0) + |Linear momentum| = 9.38987e-09 + Linear kinetic energy = 3.06338e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 397.583, 540.2 + Mass transfer phase change = 2.0314e-10 + D10, D32, Dmax (mu) = 64.2314, 89.9843, 175.304 + Liquid penetration 95% mass (m) = 0.011135 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.056366, Final residual = 1.96154e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0164144, Final residual = 5.44744e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00150196, Final residual = 6.93527e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000446933, Final residual = 3.57994e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000466092, Final residual = 3.6132e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000465929, Final residual = 3.62418e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00132328, Final residual = 6.44657e-08, No Iterations 1 +min/max(T) = 806.604, 2779.16 +GAMG: Solving for p, Initial residual = 0.141557, Final residual = 0.00348845, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.9569e-05, global = 1.68382e-05, cumulative = 0.00460639 +GAMG: Solving for p, Initial residual = 0.00369229, Final residual = 7.19441e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.67014e-05, global = 1.67009e-05, cumulative = 0.00462309 +smoothSolver: Solving for epsilon, Initial residual = 0.000919683, Final residual = 1.23392e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0010494, Final residual = 1.79366e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.108195 s +other Time = 0 s +rho Equations = 0.000179 s +U Equations = 0.001239 s +Y Equations = 0.00245699 s +E Equations = 0.000618 s +p Equations = 0.002627 s +calculate parcels = 123.826 s +chemistry correctThermo = 0.002867 s +turbulence correct = 0.001369 s +combustion correct(in Y) = 0.096624 s +percentage of chemistry = 89.3054 % +percentage of rho/U/Y/E = 4.15268 % +========Time details of each equation======= +rhoEqn Time = 0.000327 s +rhoEqn assamble = 0.000257 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001237 s +UEqn assamble = 0.000725 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000512 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001812 s +YEqn assamble = 0.000624 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000191 s +YEqn correct boundary = 0 s +EEqn Time = 0.000461 s +EEqn assamble = 0.000345 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 182.81 s ClockTime = 183 s +Courant Number mean: 0.00360341 max: 0.0165832 +Time = 0.0015475 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22327 + Current mass in system = 1.50151e-09 + Linear momentum = (1.66317e-11 -9.35995e-09 0) + |Linear momentum| = 9.35996e-09 + Linear kinetic energy = 3.04739e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 397.829, 540.2 + Mass transfer phase change = 2.04635e-10 + D10, D32, Dmax (mu) = 64.2171, 89.968, 174.999 + Liquid penetration 95% mass (m) = 0.0111495 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0544323, Final residual = 1.91821e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0155522, Final residual = 5.10123e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0015437, Final residual = 7.54825e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000444779, Final residual = 3.54968e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000463291, Final residual = 3.61616e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000463124, Final residual = 3.62799e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00132102, Final residual = 6.22165e-08, No Iterations 1 +min/max(T) = 806.647, 2777.42 +GAMG: Solving for p, Initial residual = 0.164149, Final residual = 0.00289814, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.89537e-05, global = 1.72197e-05, cumulative = 0.00464031 +GAMG: Solving for p, Initial residual = 0.0030314, Final residual = 4.0314e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.72318e-05, global = 1.72316e-05, cumulative = 0.00465754 +smoothSolver: Solving for epsilon, Initial residual = 0.000937816, Final residual = 1.29618e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00105584, Final residual = 1.84731e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.075309 s +other Time = 1e-06 s +rho Equations = 0.000178 s +U Equations = 0.0011 s +Y Equations = 0.00236295 s +E Equations = 0.000512 s +p Equations = 0.002294 s +calculate parcels = 124.121 s +chemistry correctThermo = 0.002186 s +turbulence correct = 0.000907 s +combustion correct(in Y) = 0.0655621 s +percentage of chemistry = 87.0574 % +percentage of rho/U/Y/E = 5.51454 % +========Time details of each equation======= +rhoEqn Time = 0.000309 s +rhoEqn assamble = 0.000249 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001099 s +UEqn assamble = 0.000645 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000454 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001723 s +YEqn assamble = 0.00056 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000119 s +YEqn correct boundary = 0 s +EEqn Time = 0.000383 s +EEqn assamble = 0.000284 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 183.18 s ClockTime = 184 s +Courant Number mean: 0.00361541 max: 0.0177721 +Time = 0.00155 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22321 + Current mass in system = 1.49984e-09 + Linear momentum = (1.67899e-11 -9.32822e-09 0) + |Linear momentum| = 9.32824e-09 + Linear kinetic energy = 3.03057e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 398.093, 540.2 + Mass transfer phase change = 2.06301e-10 + D10, D32, Dmax (mu) = 64.355, 89.9678, 174.695 + Liquid penetration 95% mass (m) = 0.0111654 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0559872, Final residual = 1.99402e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0147226, Final residual = 4.72452e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00172618, Final residual = 9.33853e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000442918, Final residual = 3.56001e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000467378, Final residual = 3.57851e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000467239, Final residual = 3.59021e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00133806, Final residual = 6.07166e-08, No Iterations 1 +min/max(T) = 806.682, 2775.38 +GAMG: Solving for p, Initial residual = 0.189927, Final residual = 0.00458502, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.13369e-05, global = 1.8907e-05, cumulative = 0.00467645 +GAMG: Solving for p, Initial residual = 0.00459291, Final residual = 4.48884e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.92051e-05, global = 1.92049e-05, cumulative = 0.00469565 +smoothSolver: Solving for epsilon, Initial residual = 0.000967728, Final residual = 1.3911e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00106872, Final residual = 1.92484e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.099055 s +other Time = 1e-06 s +rho Equations = 0.000163 s +U Equations = 0.001019 s +Y Equations = 0.00249054 s +E Equations = 0.000613 s +p Equations = 0.002716 s +calculate parcels = 124.462 s +chemistry correctThermo = 0.002862 s +turbulence correct = 0.00114 s +combustion correct(in Y) = 0.0878705 s +percentage of chemistry = 88.7088 % +percentage of rho/U/Y/E = 4.32643 % +========Time details of each equation======= +rhoEqn Time = 0.000322 s +rhoEqn assamble = 0.000252 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001017 s +UEqn assamble = 0.000595 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000422 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001903 s +YEqn assamble = 0.000646 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000236 s +YEqn correct boundary = 0 s +EEqn Time = 0.000454 s +EEqn assamble = 0.000341 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 183.62 s ClockTime = 184 s +Courant Number mean: 0.00363092 max: 0.0226056 +Time = 0.0015525 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22315 + Current mass in system = 1.4981e-09 + Linear momentum = (1.74597e-11 -9.29452e-09 0) + |Linear momentum| = 9.29453e-09 + Linear kinetic energy = 3.01276e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 398.359, 540.2 + Mass transfer phase change = 2.08038e-10 + D10, D32, Dmax (mu) = 64.4113, 89.9526, 174.402 + Liquid penetration 95% mass (m) = 0.0111814 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.068298, Final residual = 2.97614e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0145434, Final residual = 4.9527e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00179655, Final residual = 1.07381e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000433563, Final residual = 3.61487e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000476971, Final residual = 3.91491e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000476813, Final residual = 3.92873e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00133826, Final residual = 6.42456e-08, No Iterations 1 +min/max(T) = 806.715, 2772.56 +GAMG: Solving for p, Initial residual = 0.19732, Final residual = 0.00743826, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.38377e-05, global = 2.0093e-05, cumulative = 0.00471574 +GAMG: Solving for p, Initial residual = 0.00708219, Final residual = 4.37339e-07, No Iterations 6 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.00248e-05, global = 2.00245e-05, cumulative = 0.00473577 +smoothSolver: Solving for epsilon, Initial residual = 0.00102527, Final residual = 1.53187e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00110526, Final residual = 2.05177e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102579 s +other Time = 0 s +rho Equations = 0.00019 s +U Equations = 0.001038 s +Y Equations = 0.00213653 s +E Equations = 0.000491 s +p Equations = 0.002417 s +calculate parcels = 124.812 s +chemistry correctThermo = 0.002453 s +turbulence correct = 0.000981 s +combustion correct(in Y) = 0.0926785 s +percentage of chemistry = 90.3484 % +percentage of rho/U/Y/E = 3.7586 % +========Time details of each equation======= +rhoEqn Time = 0.000315 s +rhoEqn assamble = 0.00025 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001037 s +UEqn assamble = 0.000587 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00045 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001563 s +YEqn assamble = 0.000538 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000138 s +YEqn correct boundary = 0 s +EEqn Time = 0.000368 s +EEqn assamble = 0.000275 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 184.08 s ClockTime = 185 s +Courant Number mean: 0.00363909 max: 0.0252792 +Time = 0.001555 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22314 + Current mass in system = 1.49646e-09 + Linear momentum = (1.72479e-11 -9.25937e-09 0) + |Linear momentum| = 9.25939e-09 + Linear kinetic energy = 2.99408e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 398.618, 540.2 + Mass transfer phase change = 2.09684e-10 + D10, D32, Dmax (mu) = 64.2779, 89.9059, 174.978 + Liquid penetration 95% mass (m) = 0.0111975 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.087966, Final residual = 4.01191e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0146515, Final residual = 5.28111e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00163536, Final residual = 9.24809e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000427785, Final residual = 3.53522e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000479133, Final residual = 3.98377e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000478933, Final residual = 3.99781e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0012963, Final residual = 6.17033e-08, No Iterations 1 +min/max(T) = 806.745, 2768.49 +GAMG: Solving for p, Initial residual = 0.18581, Final residual = 0.00600023, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.32332e-05, global = 1.89709e-05, cumulative = 0.00475474 +GAMG: Solving for p, Initial residual = 0.00547083, Final residual = 6.21217e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.89648e-05, global = 1.89643e-05, cumulative = 0.0047737 +smoothSolver: Solving for epsilon, Initial residual = 0.00104993, Final residual = 1.53569e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00113388, Final residual = 2.09223e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.110122 s +other Time = 0 s +rho Equations = 0.000174 s +U Equations = 0.001252 s +Y Equations = 0.00247223 s +E Equations = 0.000706 s +p Equations = 0.002648 s +calculate parcels = 125.179 s +chemistry correctThermo = 0.002818 s +turbulence correct = 0.000999 s +combustion correct(in Y) = 0.0988038 s +percentage of chemistry = 89.7221 % +percentage of rho/U/Y/E = 4.18102 % +========Time details of each equation======= +rhoEqn Time = 0.000321 s +rhoEqn assamble = 0.000253 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001252 s +UEqn assamble = 0.000728 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000524 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001825 s +YEqn assamble = 0.000636 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000192 s +YEqn correct boundary = 0 s +EEqn Time = 0.000551 s +EEqn assamble = 0.000422 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000129 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 184.55 s ClockTime = 185 s +Courant Number mean: 0.00363366 max: 0.0284995 +Time = 0.0015575 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22314 + Current mass in system = 1.49491e-09 + Linear momentum = (1.63865e-11 -9.22388e-09 0) + |Linear momentum| = 9.2239e-09 + Linear kinetic energy = 2.97517e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 398.87, 540.2 + Mass transfer phase change = 2.11235e-10 + D10, D32, Dmax (mu) = 64.1519, 89.8531, 175.618 + Liquid penetration 95% mass (m) = 0.0112142 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0819363, Final residual = 3.7593e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0138154, Final residual = 4.5858e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00145467, Final residual = 6.51681e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000427623, Final residual = 3.55782e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000462698, Final residual = 3.7908e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000462463, Final residual = 3.80326e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00123647, Final residual = 5.61773e-08, No Iterations 1 +min/max(T) = 806.71, 2766.55 +GAMG: Solving for p, Initial residual = 0.155509, Final residual = 0.00608649, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.24809e-05, global = 1.84364e-05, cumulative = 0.00479214 +GAMG: Solving for p, Initial residual = 0.00564418, Final residual = 2.98095e-07, No Iterations 6 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.78792e-05, global = 1.7879e-05, cumulative = 0.00481002 +smoothSolver: Solving for epsilon, Initial residual = 0.00101478, Final residual = 1.42433e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0011125, Final residual = 2.00143e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.105835 s +other Time = 1e-06 s +rho Equations = 0.000175 s +U Equations = 0.001247 s +Y Equations = 0.00248463 s +E Equations = 0.000599 s +p Equations = 0.002866 s +calculate parcels = 125.527 s +chemistry correctThermo = 0.002973 s +turbulence correct = 0.001034 s +combustion correct(in Y) = 0.0942404 s +percentage of chemistry = 89.0446 % +percentage of rho/U/Y/E = 4.25723 % +========Time details of each equation======= +rhoEqn Time = 0.000324 s +rhoEqn assamble = 0.000255 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001245 s +UEqn assamble = 0.000759 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000486 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001835 s +YEqn assamble = 0.000649 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000174 s +YEqn correct boundary = 0 s +EEqn Time = 0.00044 s +EEqn assamble = 0.000329 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 185.01 s ClockTime = 186 s +Courant Number mean: 0.00361981 max: 0.0195795 +Time = 0.00156 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22314 + Current mass in system = 1.49336e-09 + Linear momentum = (1.55514e-11 -9.18912e-09 0) + |Linear momentum| = 9.18913e-09 + Linear kinetic energy = 2.95669e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 399.122, 540.2 + Mass transfer phase change = 2.12786e-10 + D10, D32, Dmax (mu) = 64.0371, 89.802, 176.232 + Liquid penetration 95% mass (m) = 0.0112305 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0735331, Final residual = 3.20404e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0144716, Final residual = 4.91699e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00144871, Final residual = 6.51575e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000422861, Final residual = 3.62181e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000455323, Final residual = 3.81204e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000455073, Final residual = 3.82455e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00121401, Final residual = 5.62422e-08, No Iterations 1 +min/max(T) = 806.678, 2764.74 +GAMG: Solving for p, Initial residual = 0.133974, Final residual = 0.00403011, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.16825e-05, global = 1.83211e-05, cumulative = 0.00482834 +GAMG: Solving for p, Initial residual = 0.00367679, Final residual = 3.15625e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.78779e-05, global = 1.78777e-05, cumulative = 0.00484622 +smoothSolver: Solving for epsilon, Initial residual = 0.000986705, Final residual = 1.38121e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00109108, Final residual = 1.9472e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.077402 s +other Time = 1e-06 s +rho Equations = 0.00019 s +U Equations = 0.001187 s +Y Equations = 0.00237997 s +E Equations = 0.000525 s +p Equations = 0.002448 s +calculate parcels = 125.853 s +chemistry correctThermo = 0.001945 s +turbulence correct = 0.001031 s +combustion correct(in Y) = 0.067485 s +percentage of chemistry = 87.1877 % +percentage of rho/U/Y/E = 5.53211 % +========Time details of each equation======= +rhoEqn Time = 0.000315 s +rhoEqn assamble = 0.00025 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001185 s +UEqn assamble = 0.000727 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000458 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001807 s +YEqn assamble = 0.000642 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000186 s +YEqn correct boundary = 0 s +EEqn Time = 0.000397 s +EEqn assamble = 0.000291 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000106 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 185.41 s ClockTime = 186 s +Courant Number mean: 0.00360359 max: 0.0198997 +Time = 0.0015625 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22314 + Current mass in system = 1.4918e-09 + Linear momentum = (1.50299e-11 -9.15514e-09 0) + |Linear momentum| = 9.15516e-09 + Linear kinetic energy = 2.93873e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 399.378, 540.2 + Mass transfer phase change = 2.14341e-10 + D10, D32, Dmax (mu) = 63.9231, 89.7517, 176.434 + Liquid penetration 95% mass (m) = 0.0112458 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0628467, Final residual = 2.43393e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0155116, Final residual = 5.3027e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00145088, Final residual = 6.64159e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000428842, Final residual = 3.76521e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000461074, Final residual = 3.94202e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000460829, Final residual = 3.95483e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00121173, Final residual = 5.71212e-08, No Iterations 1 +min/max(T) = 806.647, 2764.07 +GAMG: Solving for p, Initial residual = 0.115902, Final residual = 0.00329262, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.1295e-05, global = 1.82577e-05, cumulative = 0.00486448 +GAMG: Solving for p, Initial residual = 0.00292515, Final residual = 2.55781e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.7927e-05, global = 1.79268e-05, cumulative = 0.0048824 +smoothSolver: Solving for epsilon, Initial residual = 0.00097787, Final residual = 1.38404e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00107713, Final residual = 1.93177e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.096868 s +other Time = 0 s +rho Equations = 0.000181 s +U Equations = 0.001165 s +Y Equations = 0.00215697 s +E Equations = 0.000482 s +p Equations = 0.002104 s +calculate parcels = 126.137 s +chemistry correctThermo = 0.002004 s +turbulence correct = 0.000819 s +combustion correct(in Y) = 0.087756 s +percentage of chemistry = 90.5934 % +percentage of rho/U/Y/E = 4.11382 % +========Time details of each equation======= +rhoEqn Time = 0.000302 s +rhoEqn assamble = 0.000237 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001164 s +UEqn assamble = 0.000678 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000486 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001526 s +YEqn assamble = 0.000561 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000121 s +YEqn correct boundary = 0 s +EEqn Time = 0.000362 s +EEqn assamble = 0.000268 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 185.79 s ClockTime = 186 s +Courant Number mean: 0.00358236 max: 0.0199767 +Time = 0.001565 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22311 + Current mass in system = 1.49009e-09 + Linear momentum = (1.48042e-11 -9.12094e-09 0) + |Linear momentum| = 9.12096e-09 + Linear kinetic energy = 2.92091e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 399.644, 540.2 + Mass transfer phase change = 2.16053e-10 + D10, D32, Dmax (mu) = 63.8837, 89.7139, 176.239 + Liquid penetration 95% mass (m) = 0.0112614 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0581969, Final residual = 2.45933e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0164719, Final residual = 5.47627e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00166641, Final residual = 9.2835e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000434544, Final residual = 3.86077e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000484853, Final residual = 4.12484e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000484603, Final residual = 4.13863e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00125286, Final residual = 6.12758e-08, No Iterations 1 +min/max(T) = 806.617, 2763.38 +GAMG: Solving for p, Initial residual = 0.100085, Final residual = 0.00369254, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.27362e-05, global = 1.97028e-05, cumulative = 0.00490211 +GAMG: Solving for p, Initial residual = 0.00326915, Final residual = 3.40863e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.97269e-05, global = 1.97267e-05, cumulative = 0.00492183 +smoothSolver: Solving for epsilon, Initial residual = 0.00100264, Final residual = 1.45129e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0010798, Final residual = 1.96901e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.101951 s +other Time = 0 s +rho Equations = 0.000196 s +U Equations = 0.001235 s +Y Equations = 0.00247376 s +E Equations = 0.000602 s +p Equations = 0.002677 s +calculate parcels = 126.485 s +chemistry correctThermo = 0.002862 s +turbulence correct = 0.001132 s +combustion correct(in Y) = 0.0905642 s +percentage of chemistry = 88.8311 % +percentage of rho/U/Y/E = 4.42052 % +========Time details of each equation======= +rhoEqn Time = 0.000353 s +rhoEqn assamble = 0.000267 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001234 s +UEqn assamble = 0.000723 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000511 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00181 s +YEqn assamble = 0.000658 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000173 s +YEqn correct boundary = 0 s +EEqn Time = 0.000445 s +EEqn assamble = 0.000331 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 186.24 s ClockTime = 187 s +Courant Number mean: 0.00357133 max: 0.0269382 +Time = 0.0015675 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22307 + Current mass in system = 1.48839e-09 + Linear momentum = (1.54057e-11 -9.08586e-09 0) + |Linear momentum| = 9.08588e-09 + Linear kinetic energy = 2.90269e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 399.914, 540.2 + Mass transfer phase change = 2.17748e-10 + D10, D32, Dmax (mu) = 63.9189, 89.6752, 176.816 + Liquid penetration 95% mass (m) = 0.0112768 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0782138, Final residual = 4.04548e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0176583, Final residual = 5.89889e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00161266, Final residual = 8.2126e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000436978, Final residual = 4.00148e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000467852, Final residual = 4.05592e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000467598, Final residual = 4.06934e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00125102, Final residual = 6.22944e-08, No Iterations 1 +min/max(T) = 806.589, 2761.84 +GAMG: Solving for p, Initial residual = 0.0880175, Final residual = 0.00291904, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.30088e-05, global = 1.9684e-05, cumulative = 0.00494152 +GAMG: Solving for p, Initial residual = 0.00262138, Final residual = 3.98838e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.95407e-05, global = 1.95401e-05, cumulative = 0.00496106 +smoothSolver: Solving for epsilon, Initial residual = 0.0010377, Final residual = 1.55281e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00110296, Final residual = 2.066e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.080229 s +other Time = 0 s +rho Equations = 0.000156 s +U Equations = 0.000983 s +Y Equations = 0.00222376 s +E Equations = 0.000502 s +p Equations = 0.003086 s +calculate parcels = 126.836 s +chemistry correctThermo = 0.002036 s +turbulence correct = 0.001198 s +combustion correct(in Y) = 0.0698592 s +percentage of chemistry = 87.0748 % +percentage of rho/U/Y/E = 4.81716 % +========Time details of each equation======= +rhoEqn Time = 0.000462 s +rhoEqn assamble = 0.000372 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000982 s +UEqn assamble = 0.000575 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000407 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001668 s +YEqn assamble = 0.000586 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000154 s +YEqn correct boundary = 0 s +EEqn Time = 0.000373 s +EEqn assamble = 0.00028 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 186.67 s ClockTime = 187 s +Courant Number mean: 0.00355256 max: 0.0230073 +Time = 0.00157 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22297 + Current mass in system = 1.48639e-09 + Linear momentum = (1.67538e-11 -9.04858e-09 0) + |Linear momentum| = 9.0486e-09 + Linear kinetic energy = 2.88362e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 400.187, 540.2 + Mass transfer phase change = 2.19755e-10 + D10, D32, Dmax (mu) = 64.0743, 89.6567, 177.416 + Liquid penetration 95% mass (m) = 0.0112924 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0712928, Final residual = 3.06869e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0184044, Final residual = 6.12298e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00193679, Final residual = 1.41125e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000437186, Final residual = 4.07503e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000490553, Final residual = 4.52387e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000490267, Final residual = 4.53935e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0012876, Final residual = 7.17765e-08, No Iterations 1 +min/max(T) = 806.561, 2759.47 +GAMG: Solving for p, Initial residual = 0.0779064, Final residual = 0.00430298, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.87836e-05, global = 2.306e-05, cumulative = 0.00498412 +GAMG: Solving for p, Initial residual = 0.0039285, Final residual = 2.95701e-07, No Iterations 6 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.3128e-05, global = 2.31275e-05, cumulative = 0.00500724 +smoothSolver: Solving for epsilon, Initial residual = 0.00112894, Final residual = 1.77787e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00115937, Final residual = 2.2547e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.10378 s +other Time = 0 s +rho Equations = 0.000162 s +U Equations = 0.001127 s +Y Equations = 0.00243804 s +E Equations = 0.000606 s +p Equations = 0.00279 s +calculate parcels = 127.172 s +chemistry correctThermo = 0.002829 s +turbulence correct = 0.001021 s +combustion correct(in Y) = 0.092596 s +percentage of chemistry = 89.2233 % +percentage of rho/U/Y/E = 4.17522 % +========Time details of each equation======= +rhoEqn Time = 0.000307 s +rhoEqn assamble = 0.000241 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001126 s +UEqn assamble = 0.000685 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000441 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001869 s +YEqn assamble = 0.000648 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000227 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 187.11 s ClockTime = 188 s +Courant Number mean: 0.00354576 max: 0.0358068 +Time = 0.0015725 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22293 + Current mass in system = 1.48457e-09 + Linear momentum = (1.67048e-11 -9.0095e-09 0) + |Linear momentum| = 9.00952e-09 + Linear kinetic energy = 2.86351e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 400.455, 540.2 + Mass transfer phase change = 2.21578e-10 + D10, D32, Dmax (mu) = 64.0156, 89.5976, 178.029 + Liquid penetration 95% mass (m) = 0.0113061 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0963652, Final residual = 4.63778e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0215692, Final residual = 8.20004e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00170434, Final residual = 9.81143e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00043977, Final residual = 4.03258e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000494595, Final residual = 4.44759e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000494339, Final residual = 4.46234e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00125307, Final residual = 6.72624e-08, No Iterations 1 +min/max(T) = 806.535, 2757.27 +GAMG: Solving for p, Initial residual = 0.0741584, Final residual = 0.00418904, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.67859e-05, global = 2.13241e-05, cumulative = 0.00502857 +GAMG: Solving for p, Initial residual = 0.00382893, Final residual = 2.4845e-07, No Iterations 6 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.10116e-05, global = 2.10113e-05, cumulative = 0.00504958 +smoothSolver: Solving for epsilon, Initial residual = 0.00114128, Final residual = 1.71531e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00117289, Final residual = 2.24468e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.086692 s +other Time = 1e-06 s +rho Equations = 0.00021 s +U Equations = 0.001348 s +Y Equations = 0.00214162 s +E Equations = 0.000487 s +p Equations = 0.002918 s +calculate parcels = 127.553 s +chemistry correctThermo = 0.002066 s +turbulence correct = 0.000913 s +combustion correct(in Y) = 0.0763884 s +percentage of chemistry = 88.1147 % +percentage of rho/U/Y/E = 4.82931 % +========Time details of each equation======= +rhoEqn Time = 0.000347 s +rhoEqn assamble = 0.000269 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001347 s +UEqn assamble = 0.000806 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000541 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001403 s +YEqn assamble = 0.000523 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 5e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000367 s +EEqn assamble = 0.000274 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 187.58 s ClockTime = 188 s +Courant Number mean: 0.0035158 max: 0.0280587 +Time = 0.001575 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22291 + Current mass in system = 1.48283e-09 + Linear momentum = (1.65597e-11 -8.96965e-09 0) + |Linear momentum| = 8.96967e-09 + Linear kinetic energy = 2.84294e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 400.741, 540.2 + Mass transfer phase change = 2.23317e-10 + D10, D32, Dmax (mu) = 63.915, 89.5276, 178.658 + Liquid penetration 95% mass (m) = 0.011321 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0861677, Final residual = 3.88378e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.021732, Final residual = 7.54658e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00152424, Final residual = 7.84127e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000440898, Final residual = 4.13048e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000479885, Final residual = 4.40657e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000479592, Final residual = 4.42066e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00120419, Final residual = 6.65883e-08, No Iterations 1 +min/max(T) = 806.509, 2756.6 +GAMG: Solving for p, Initial residual = 0.0612158, Final residual = 0.00317265, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.63548e-05, global = 2.0656e-05, cumulative = 0.00507024 +GAMG: Solving for p, Initial residual = 0.00295971, Final residual = 1.99921e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.00519e-05, global = 2.00515e-05, cumulative = 0.00509029 +smoothSolver: Solving for epsilon, Initial residual = 0.00112143, Final residual = 1.647e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0011632, Final residual = 2.1792e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.075067 s +other Time = 1e-06 s +rho Equations = 0.000168 s +U Equations = 0.001113 s +Y Equations = 0.00226917 s +E Equations = 0.000499 s +p Equations = 0.002246 s +calculate parcels = 127.841 s +chemistry correctThermo = 0.002415 s +turbulence correct = 0.000841 s +combustion correct(in Y) = 0.0653208 s +percentage of chemistry = 87.0167 % +percentage of rho/U/Y/E = 5.39407 % +========Time details of each equation======= +rhoEqn Time = 0.000294 s +rhoEqn assamble = 0.000232 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001113 s +UEqn assamble = 0.000681 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000432 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001699 s +YEqn assamble = 0.000652 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000132 s +YEqn correct boundary = 0 s +EEqn Time = 0.000376 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 187.94 s ClockTime = 188 s +Courant Number mean: 0.00347529 max: 0.0224632 +Time = 0.0015775 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22290 + Current mass in system = 1.4811e-09 + Linear momentum = (1.64782e-11 -8.93055e-09 0) + |Linear momentum| = 8.93056e-09 + Linear kinetic energy = 2.82277e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 401.023, 540.2 + Mass transfer phase change = 2.25045e-10 + D10, D32, Dmax (mu) = 63.7787, 89.4513, 179.306 + Liquid penetration 95% mass (m) = 0.0113352 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.082367, Final residual = 3.16142e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0232663, Final residual = 8.17759e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00152733, Final residual = 7.95644e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000437539, Final residual = 4.25134e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000489118, Final residual = 4.51686e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000488838, Final residual = 4.532e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0011802, Final residual = 6.75627e-08, No Iterations 1 +min/max(T) = 806.483, 2756.24 +GAMG: Solving for p, Initial residual = 0.0499944, Final residual = 0.00234915, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.44592e-05, global = 2.03466e-05, cumulative = 0.00511063 +GAMG: Solving for p, Initial residual = 0.00216017, Final residual = 2.07195e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.99127e-05, global = 1.99123e-05, cumulative = 0.00513055 +smoothSolver: Solving for epsilon, Initial residual = 0.00108056, Final residual = 1.5842e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00112879, Final residual = 2.09804e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.108882 s +other Time = 1e-06 s +rho Equations = 0.000169 s +U Equations = 0.001218 s +Y Equations = 0.00272881 s +E Equations = 0.000681 s +p Equations = 0.002925 s +calculate parcels = 128.173 s +chemistry correctThermo = 0.003038 s +turbulence correct = 0.001117 s +combustion correct(in Y) = 0.0967962 s +percentage of chemistry = 88.9001 % +percentage of rho/U/Y/E = 4.40551 % +========Time details of each equation======= +rhoEqn Time = 0.000335 s +rhoEqn assamble = 0.000263 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001217 s +UEqn assamble = 0.000685 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000532 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002063 s +YEqn assamble = 0.000719 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000247 s +YEqn correct boundary = 0 s +EEqn Time = 0.000509 s +EEqn assamble = 0.000349 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00016 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 188.39 s ClockTime = 189 s +Courant Number mean: 0.00343322 max: 0.022235 +Time = 0.00158 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22289 + Current mass in system = 1.47935e-09 + Linear momentum = (1.66526e-11 -8.89268e-09 0) + |Linear momentum| = 8.89269e-09 + Linear kinetic energy = 2.80337e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 401.321, 540.2 + Mass transfer phase change = 2.26793e-10 + D10, D32, Dmax (mu) = 63.6492, 89.3779, 179.967 + Liquid penetration 95% mass (m) = 0.0113492 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0691001, Final residual = 2.38371e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0247156, Final residual = 8.61444e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00152574, Final residual = 7.89957e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000437654, Final residual = 4.24677e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000480712, Final residual = 4.40373e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000480496, Final residual = 4.41896e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00115894, Final residual = 6.5968e-08, No Iterations 1 +min/max(T) = 806.458, 2755.84 +GAMG: Solving for p, Initial residual = 0.0442728, Final residual = 0.00209625, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.45603e-05, global = 2.05985e-05, cumulative = 0.00515114 +GAMG: Solving for p, Initial residual = 0.00193333, Final residual = 2.47655e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.01412e-05, global = 2.01406e-05, cumulative = 0.00517128 +smoothSolver: Solving for epsilon, Initial residual = 0.00107731, Final residual = 1.60346e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00111846, Final residual = 2.09438e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.104378 s +other Time = 0 s +rho Equations = 0.000179 s +U Equations = 0.001208 s +Y Equations = 0.00239332 s +E Equations = 0.000602 s +p Equations = 0.002109 s +calculate parcels = 128.537 s +chemistry correctThermo = 0.003213 s +turbulence correct = 0.000793 s +combustion correct(in Y) = 0.0936487 s +percentage of chemistry = 89.7207 % +percentage of rho/U/Y/E = 4.19851 % +========Time details of each equation======= +rhoEqn Time = 0.000301 s +rhoEqn assamble = 0.000237 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001207 s +UEqn assamble = 0.000705 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000502 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001742 s +YEqn assamble = 0.000618 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000177 s +YEqn correct boundary = 0 s +EEqn Time = 0.000441 s +EEqn assamble = 0.00033 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 188.85 s ClockTime = 189 s +Courant Number mean: 0.00338892 max: 0.0227243 +Time = 0.0015825 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22287 + Current mass in system = 1.47755e-09 + Linear momentum = (1.66233e-11 -8.85505e-09 0) + |Linear momentum| = 8.85507e-09 + Linear kinetic energy = 2.78425e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 401.639, 540.2 + Mass transfer phase change = 2.28592e-10 + D10, D32, Dmax (mu) = 63.5383, 89.3063, 180.624 + Liquid penetration 95% mass (m) = 0.0113631 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0547322, Final residual = 2.01809e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0256809, Final residual = 8.53085e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00158686, Final residual = 8.04736e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000431833, Final residual = 4.16247e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000474393, Final residual = 4.24158e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000474202, Final residual = 4.25624e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00116175, Final residual = 6.42093e-08, No Iterations 1 +min/max(T) = 806.432, 2755.36 +GAMG: Solving for p, Initial residual = 0.0407962, Final residual = 0.00190693, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.45075e-05, global = 2.10799e-05, cumulative = 0.00519236 +GAMG: Solving for p, Initial residual = 0.00176185, Final residual = 2.11543e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.07388e-05, global = 2.07385e-05, cumulative = 0.0052131 +smoothSolver: Solving for epsilon, Initial residual = 0.00109743, Final residual = 1.66558e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00112481, Final residual = 2.1448e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094927 s +other Time = 0 s +rho Equations = 0.000194 s +U Equations = 0.001419 s +Y Equations = 0.00210324 s +E Equations = 0.000519 s +p Equations = 0.002037 s +calculate parcels = 128.873 s +chemistry correctThermo = 0.002035 s +turbulence correct = 0.000791 s +combustion correct(in Y) = 0.0856268 s +percentage of chemistry = 90.2028 % +percentage of rho/U/Y/E = 4.46157 % +========Time details of each equation======= +rhoEqn Time = 0.000308 s +rhoEqn assamble = 0.000242 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001418 s +UEqn assamble = 0.000876 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000542 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00137 s +YEqn assamble = 0.000503 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 4.6e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000401 s +EEqn assamble = 0.000302 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 189.29 s ClockTime = 190 s +Courant Number mean: 0.00333854 max: 0.0243295 +Time = 0.001585 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22283 + Current mass in system = 1.47563e-09 + Linear momentum = (1.69071e-11 -8.81661e-09 0) + |Linear momentum| = 8.81663e-09 + Linear kinetic energy = 2.76491e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 401.966, 540.2 + Mass transfer phase change = 2.30512e-10 + D10, D32, Dmax (mu) = 63.5052, 89.2354, 181.27 + Liquid penetration 95% mass (m) = 0.0113769 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0471988, Final residual = 2.02089e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0274128, Final residual = 8.87456e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00169111, Final residual = 1.01412e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000429394, Final residual = 4.17504e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000487767, Final residual = 4.37292e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000487547, Final residual = 4.3879e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00117863, Final residual = 6.8581e-08, No Iterations 1 +min/max(T) = 806.407, 2754.96 +GAMG: Solving for p, Initial residual = 0.0377377, Final residual = 0.00145235, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.48704e-05, global = 2.21987e-05, cumulative = 0.0052353 +GAMG: Solving for p, Initial residual = 0.00135137, Final residual = 4.27855e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.21258e-05, global = 2.21249e-05, cumulative = 0.00525743 +smoothSolver: Solving for epsilon, Initial residual = 0.00114831, Final residual = 1.74556e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00115298, Final residual = 2.22277e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.101779 s +other Time = 0 s +rho Equations = 0.000187 s +U Equations = 0.001256 s +Y Equations = 0.00252297 s +E Equations = 0.000625 s +p Equations = 0.002418 s +calculate parcels = 129.228 s +chemistry correctThermo = 0.002889 s +turbulence correct = 0.000982 s +combustion correct(in Y) = 0.090647 s +percentage of chemistry = 89.0626 % +percentage of rho/U/Y/E = 4.51073 % +========Time details of each equation======= +rhoEqn Time = 0.000332 s +rhoEqn assamble = 0.000258 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001255 s +UEqn assamble = 0.000762 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000493 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001858 s +YEqn assamble = 0.000657 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000197 s +YEqn correct boundary = 0 s +EEqn Time = 0.000466 s +EEqn assamble = 0.000349 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 189.74 s ClockTime = 190 s +Courant Number mean: 0.0032842 max: 0.0322219 +Time = 0.0015875 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22281 + Current mass in system = 1.47376e-09 + Linear momentum = (1.75314e-11 -8.7772e-09 0) + |Linear momentum| = 8.77721e-09 + Linear kinetic energy = 2.74512e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 402.291, 540.2 + Mass transfer phase change = 2.32386e-10 + D10, D32, Dmax (mu) = 63.3544, 89.1501, 181.896 + Liquid penetration 95% mass (m) = 0.0113913 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0516208, Final residual = 2.61146e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0293994, Final residual = 9.98783e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00157398, Final residual = 8.80504e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000432618, Final residual = 4.27047e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000485745, Final residual = 4.57886e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000485483, Final residual = 4.59407e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00115192, Final residual = 6.74917e-08, No Iterations 1 +min/max(T) = 806.382, 2754.48 +GAMG: Solving for p, Initial residual = 0.0338192, Final residual = 0.00164884, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.61012e-05, global = 2.19647e-05, cumulative = 0.00527939 +GAMG: Solving for p, Initial residual = 0.00155722, Final residual = 3.4716e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.16052e-05, global = 2.16042e-05, cumulative = 0.005301 +smoothSolver: Solving for epsilon, Initial residual = 0.0011715, Final residual = 1.79217e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00116508, Final residual = 2.25909e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.088703 s +other Time = 0 s +rho Equations = 0.000204 s +U Equations = 0.001319 s +Y Equations = 0.00232575 s +E Equations = 0.000528 s +p Equations = 0.002153 s +calculate parcels = 129.593 s +chemistry correctThermo = 0.002011 s +turbulence correct = 0.000886 s +combustion correct(in Y) = 0.0790662 s +percentage of chemistry = 89.1359 % +percentage of rho/U/Y/E = 4.93416 % +========Time details of each equation======= +rhoEqn Time = 0.000326 s +rhoEqn assamble = 0.00026 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001319 s +UEqn assamble = 0.000812 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000507 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00165 s +YEqn assamble = 0.000553 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000145 s +YEqn correct boundary = 0 s +EEqn Time = 0.000394 s +EEqn assamble = 0.000295 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 190.2 s ClockTime = 191 s +Courant Number mean: 0.00322116 max: 0.0305892 +Time = 0.00159 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22280 + Current mass in system = 1.47191e-09 + Linear momentum = (1.7818e-11 -8.73734e-09 0) + |Linear momentum| = 8.73736e-09 + Linear kinetic energy = 2.72517e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 402.611, 540.2 + Mass transfer phase change = 2.3423e-10 + D10, D32, Dmax (mu) = 63.205, 89.0575, 182.493 + Liquid penetration 95% mass (m) = 0.0114045 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0569935, Final residual = 2.60681e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0314255, Final residual = 1.04778e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00152845, Final residual = 8.33307e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000424502, Final residual = 4.16436e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000487844, Final residual = 4.56645e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000487554, Final residual = 4.58145e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00111472, Final residual = 6.67029e-08, No Iterations 1 +min/max(T) = 806.357, 2753.96 +GAMG: Solving for p, Initial residual = 0.0300813, Final residual = 0.00118829, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.46715e-05, global = 2.15266e-05, cumulative = 0.00532252 +GAMG: Solving for p, Initial residual = 0.00110926, Final residual = 4.96452e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.12522e-05, global = 2.1251e-05, cumulative = 0.00534377 +smoothSolver: Solving for epsilon, Initial residual = 0.00116572, Final residual = 1.76957e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00116087, Final residual = 2.23523e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.112283 s +other Time = 0 s +rho Equations = 0.000223 s +U Equations = 0.001192 s +Y Equations = 0.00277126 s +E Equations = 0.000691 s +p Equations = 0.00242 s +calculate parcels = 129.854 s +chemistry correctThermo = 0.003 s +turbulence correct = 0.000937 s +combustion correct(in Y) = 0.100834 s +percentage of chemistry = 89.8032 % +percentage of rho/U/Y/E = 4.34372 % +========Time details of each equation======= +rhoEqn Time = 0.000367 s +rhoEqn assamble = 0.000288 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001192 s +UEqn assamble = 0.000768 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000424 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002206 s +YEqn assamble = 0.000745 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000304 s +YEqn correct boundary = 0 s +EEqn Time = 0.000519 s +EEqn assamble = 0.0004 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000119 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 190.57 s ClockTime = 191 s +Courant Number mean: 0.00314576 max: 0.0293709 +Time = 0.0015925 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22279 + Current mass in system = 1.4701e-09 + Linear momentum = (1.76749e-11 -8.69803e-09 0) + |Linear momentum| = 8.69805e-09 + Linear kinetic energy = 2.70561e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 402.928, 540.2 + Mass transfer phase change = 2.36047e-10 + D10, D32, Dmax (mu) = 63.0807, 88.9658, 182.934 + Liquid penetration 95% mass (m) = 0.0114179 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0517533, Final residual = 2.20428e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0331885, Final residual = 1.06004e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00148413, Final residual = 7.70446e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000420552, Final residual = 4.11606e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00047332, Final residual = 4.35102e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000473051, Final residual = 4.36513e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00108456, Final residual = 6.50969e-08, No Iterations 1 +min/max(T) = 806.333, 2753.72 +GAMG: Solving for p, Initial residual = 0.027628, Final residual = 0.00110253, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.41618e-05, global = 2.13285e-05, cumulative = 0.0053651 +GAMG: Solving for p, Initial residual = 0.00104463, Final residual = 9.13919e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.09448e-05, global = 2.0943e-05, cumulative = 0.00538604 +smoothSolver: Solving for epsilon, Initial residual = 0.00112682, Final residual = 1.69522e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00113129, Final residual = 2.15161e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092252 s +other Time = 1e-06 s +rho Equations = 0.000152 s +U Equations = 0.001076 s +Y Equations = 0.00245755 s +E Equations = 0.00061 s +p Equations = 0.002394 s +calculate parcels = 130.199 s +chemistry correctThermo = 0.002799 s +turbulence correct = 0.000937 s +combustion correct(in Y) = 0.0816005 s +percentage of chemistry = 88.4539 % +percentage of rho/U/Y/E = 4.65632 % +========Time details of each equation======= +rhoEqn Time = 0.000298 s +rhoEqn assamble = 0.000234 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001074 s +UEqn assamble = 0.000659 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000415 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001906 s +YEqn assamble = 0.000669 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000234 s +YEqn correct boundary = 0 s +EEqn Time = 0.000452 s +EEqn assamble = 0.000338 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 191.01 s ClockTime = 192 s +Courant Number mean: 0.00306414 max: 0.0228894 +Time = 0.001595 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22278 + Current mass in system = 1.46826e-09 + Linear momentum = (1.72606e-11 -8.66012e-09 0) + |Linear momentum| = 8.66013e-09 + Linear kinetic energy = 2.68685e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 403.245, 540.2 + Mass transfer phase change = 2.37882e-10 + D10, D32, Dmax (mu) = 62.9422, 88.8732, 182.667 + Liquid penetration 95% mass (m) = 0.0114316 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0499598, Final residual = 2.01808e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0348552, Final residual = 1.09504e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00151154, Final residual = 8.59545e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000414684, Final residual = 4.05695e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00047404, Final residual = 4.39296e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000473758, Final residual = 4.40709e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00107359, Final residual = 6.61857e-08, No Iterations 1 +min/max(T) = 806.309, 2753.83 +GAMG: Solving for p, Initial residual = 0.0262559, Final residual = 0.000999457, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.447e-05, global = 2.13009e-05, cumulative = 0.00540735 +GAMG: Solving for p, Initial residual = 0.00095268, Final residual = 4.5427e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.11522e-05, global = 2.11506e-05, cumulative = 0.0054285 +smoothSolver: Solving for epsilon, Initial residual = 0.00111072, Final residual = 1.66417e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00111369, Final residual = 2.09813e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09646 s +other Time = 0 s +rho Equations = 0.000156 s +U Equations = 0.001112 s +Y Equations = 0.00289176 s +E Equations = 0.000603 s +p Equations = 0.002797 s +calculate parcels = 130.579 s +chemistry correctThermo = 0.002507 s +turbulence correct = 0.001156 s +combustion correct(in Y) = 0.0850142 s +percentage of chemistry = 88.1342 % +percentage of rho/U/Y/E = 4.93755 % +========Time details of each equation======= +rhoEqn Time = 0.000319 s +rhoEqn assamble = 0.000253 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001112 s +UEqn assamble = 0.000677 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000435 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002342 s +YEqn assamble = 0.000773 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000332 s +YEqn correct boundary = 0 s +EEqn Time = 0.000451 s +EEqn assamble = 0.000342 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000109 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 191.48 s ClockTime = 192 s +Courant Number mean: 0.00297916 max: 0.0264074 +Time = 0.0015975 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22276 + Current mass in system = 1.46647e-09 + Linear momentum = (1.65974e-11 -8.62339e-09 0) + |Linear momentum| = 8.62341e-09 + Linear kinetic energy = 2.66882e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 403.566, 540.2 + Mass transfer phase change = 2.39671e-10 + D10, D32, Dmax (mu) = 62.8973, 88.7807, 182.401 + Liquid penetration 95% mass (m) = 0.0114452 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0452651, Final residual = 1.80251e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0363964, Final residual = 1.11888e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00145321, Final residual = 7.28174e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000416504, Final residual = 4.05166e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000459933, Final residual = 4.17334e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000459705, Final residual = 4.18658e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00105144, Final residual = 6.26568e-08, No Iterations 1 +min/max(T) = 806.285, 2754.13 +GAMG: Solving for p, Initial residual = 0.0242105, Final residual = 0.000985965, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.34049e-05, global = 2.09902e-05, cumulative = 0.00544949 +GAMG: Solving for p, Initial residual = 0.000950204, Final residual = 8.82042e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.06248e-05, global = 2.06229e-05, cumulative = 0.00547011 +smoothSolver: Solving for epsilon, Initial residual = 0.00110021, Final residual = 1.64605e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00110611, Final residual = 2.07652e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.08874 s +other Time = 0 s +rho Equations = 0.000174 s +U Equations = 0.001182 s +Y Equations = 0.00212619 s +E Equations = 0.000516 s +p Equations = 0.002006 s +calculate parcels = 130.906 s +chemistry correctThermo = 0.001999 s +turbulence correct = 0.00089 s +combustion correct(in Y) = 0.0796428 s +percentage of chemistry = 89.7485 % +percentage of rho/U/Y/E = 4.50551 % +========Time details of each equation======= +rhoEqn Time = 0.000316 s +rhoEqn assamble = 0.00025 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001182 s +UEqn assamble = 0.000685 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000497 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.0015 s +YEqn assamble = 0.000522 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000144 s +YEqn correct boundary = 0 s +EEqn Time = 0.000383 s +EEqn assamble = 0.000285 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 191.9 s ClockTime = 192 s +Courant Number mean: 0.00289583 max: 0.0214506 +Time = 0.0016 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22274 + Current mass in system = 1.46464e-09 + Linear momentum = (1.60707e-11 -8.58735e-09 0) + |Linear momentum| = 8.58737e-09 + Linear kinetic energy = 2.65125e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 403.889, 540.2 + Mass transfer phase change = 2.41503e-10 + D10, D32, Dmax (mu) = 62.7728, 88.6905, 182.129 + Liquid penetration 95% mass (m) = 0.0114592 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0490589, Final residual = 2.19644e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0398601, Final residual = 1.24175e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00148831, Final residual = 7.81268e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00042264, Final residual = 4.09887e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000471133, Final residual = 4.25736e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000470926, Final residual = 4.27149e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00104637, Final residual = 6.26428e-08, No Iterations 1 +min/max(T) = 806.263, 2754.43 +GAMG: Solving for p, Initial residual = 0.022936, Final residual = 0.000806469, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.36936e-05, global = 2.11994e-05, cumulative = 0.00549131 +GAMG: Solving for p, Initial residual = 0.000773489, Final residual = 4.09736e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.11128e-05, global = 2.11117e-05, cumulative = 0.00551242 +smoothSolver: Solving for epsilon, Initial residual = 0.00110161, Final residual = 1.64292e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00110199, Final residual = 2.0597e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.10638 s +other Time = 0 s +rho Equations = 0.000153 s +U Equations = 0.001106 s +Y Equations = 0.00235458 s +E Equations = 0.000595 s +p Equations = 0.002455 s +calculate parcels = 131.274 s +chemistry correctThermo = 0.002847 s +turbulence correct = 0.000952 s +combustion correct(in Y) = 0.0956974 s +percentage of chemistry = 89.9581 % +percentage of rho/U/Y/E = 3.95618 % +========Time details of each equation======= +rhoEqn Time = 0.000297 s +rhoEqn assamble = 0.000236 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001104 s +UEqn assamble = 0.000688 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000416 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001811 s +YEqn assamble = 0.000627 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000222 s +YEqn correct boundary = 0 s +EEqn Time = 0.000439 s +EEqn assamble = 0.000326 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 192.68 s ClockTime = 193 s +Courant Number mean: 0.00281651 max: 0.0212181 +Time = 0.0016025 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22270 + Current mass in system = 1.46271e-09 + Linear momentum = (1.57005e-11 -8.55125e-09 0) + |Linear momentum| = 8.55126e-09 + Linear kinetic energy = 2.63381e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 404.233, 540.2 + Mass transfer phase change = 2.43435e-10 + D10, D32, Dmax (mu) = 62.639, 88.6022, 181.844 + Liquid penetration 95% mass (m) = 0.0114719 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0583961, Final residual = 2.37978e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0441114, Final residual = 1.37047e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00165458, Final residual = 1.06669e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000434625, Final residual = 4.16577e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000503739, Final residual = 4.37656e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000503501, Final residual = 4.39179e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00108574, Final residual = 6.83628e-08, No Iterations 1 +min/max(T) = 806.241, 2754.47 +GAMG: Solving for p, Initial residual = 0.0225433, Final residual = 0.00111548, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.56022e-05, global = 2.22343e-05, cumulative = 0.00553465 +GAMG: Solving for p, Initial residual = 0.00107135, Final residual = 2.0663e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.22755e-05, global = 2.2275e-05, cumulative = 0.00555693 +smoothSolver: Solving for epsilon, Initial residual = 0.00113943, Final residual = 1.69406e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00111951, Final residual = 2.08791e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.117168 s +other Time = 0 s +rho Equations = 0.000181 s +U Equations = 0.001258 s +Y Equations = 0.00244576 s +E Equations = 0.000602 s +p Equations = 0.00256 s +calculate parcels = 131.569 s +chemistry correctThermo = 0.002877 s +turbulence correct = 0.000972 s +combustion correct(in Y) = 0.106074 s +percentage of chemistry = 90.5317 % +percentage of rho/U/Y/E = 3.82934 % +========Time details of each equation======= +rhoEqn Time = 0.000321 s +rhoEqn assamble = 0.000253 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001257 s +UEqn assamble = 0.000765 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000492 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001804 s +YEqn assamble = 0.000631 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000191 s +YEqn correct boundary = 0 s +EEqn Time = 0.000446 s +EEqn assamble = 0.000334 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 193.1 s ClockTime = 194 s +Courant Number mean: 0.00276116 max: 0.0271286 +Time = 0.001605 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22246 + Current mass in system = 1.46028e-09 + Linear momentum = (1.60065e-11 -8.51247e-09 0) + |Linear momentum| = 8.51248e-09 + Linear kinetic energy = 2.61564e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 404.657, 540.2 + Mass transfer phase change = 2.45863e-10 + D10, D32, Dmax (mu) = 62.7804, 88.5833, 181.541 + Liquid penetration 95% mass (m) = 0.0114845 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0769524, Final residual = 2.66803e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0494847, Final residual = 1.53041e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00221255, Final residual = 1.61227e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000453135, Final residual = 4.31195e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000577221, Final residual = 5.08738e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000577095, Final residual = 5.1061e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00115387, Final residual = 7.06405e-08, No Iterations 1 +min/max(T) = 806.22, 2754 +GAMG: Solving for p, Initial residual = 0.0253781, Final residual = 0.00240401, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.38804e-05, global = 2.87185e-05, cumulative = 0.00558565 +GAMG: Solving for p, Initial residual = 0.00232026, Final residual = 5.73383e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.79823e-05, global = 2.79805e-05, cumulative = 0.00561363 +smoothSolver: Solving for epsilon, Initial residual = 0.00127522, Final residual = 1.93524e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00120267, Final residual = 2.26953e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.101339 s +other Time = 0 s +rho Equations = 0.000186 s +U Equations = 0.001345 s +Y Equations = 0.00250851 s +E Equations = 0.000624 s +p Equations = 0.002581 s +calculate parcels = 131.935 s +chemistry correctThermo = 0.002858 s +turbulence correct = 0.001031 s +combustion correct(in Y) = 0.0899695 s +percentage of chemistry = 88.7807 % +percentage of rho/U/Y/E = 4.60189 % +========Time details of each equation======= +rhoEqn Time = 0.000328 s +rhoEqn assamble = 0.000258 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001344 s +UEqn assamble = 0.00079 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000554 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001799 s +YEqn assamble = 0.000643 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000154 s +YEqn correct boundary = 0 s +EEqn Time = 0.000463 s +EEqn assamble = 0.00034 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000123 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 193.56 s ClockTime = 194 s +Courant Number mean: 0.0027837 max: 0.0362525 +Time = 0.0016075 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22175 + Current mass in system = 1.45635e-09 + Linear momentum = (1.62333e-11 -8.46577e-09 0) + |Linear momentum| = 8.46579e-09 + Linear kinetic energy = 2.59493e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 404.96, 540.2 + Mass transfer phase change = 2.49789e-10 + D10, D32, Dmax (mu) = 63.618, 88.7435, 181.277 + Liquid penetration 95% mass (m) = 0.0114979 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.11663, Final residual = 5.92764e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0577596, Final residual = 2.00319e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00383741, Final residual = 3.54302e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000514922, Final residual = 4.62448e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000798617, Final residual = 7.55683e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000798555, Final residual = 7.58525e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00138776, Final residual = 9.73844e-08, No Iterations 1 +min/max(T) = 806.2, 2751.4 +GAMG: Solving for p, Initial residual = 0.0355779, Final residual = 0.000673423, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.68821e-05, global = 4.45253e-05, cumulative = 0.00565815 +GAMG: Solving for p, Initial residual = 0.000618651, Final residual = 3.25608e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.52466e-05, global = 4.52455e-05, cumulative = 0.0057034 +smoothSolver: Solving for epsilon, Initial residual = 0.001978, Final residual = 4.33798e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00164154, Final residual = 4.35654e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.111675 s +other Time = 1e-06 s +rho Equations = 0.000211 s +U Equations = 0.001473 s +Y Equations = 0.00251026 s +E Equations = 0.000644 s +p Equations = 0.002774 s +calculate parcels = 132.272 s +chemistry correctThermo = 0.002897 s +turbulence correct = 0.000984 s +combustion correct(in Y) = 0.0999507 s +percentage of chemistry = 89.5014 % +percentage of rho/U/Y/E = 4.33245 % +========Time details of each equation======= +rhoEqn Time = 0.00037 s +rhoEqn assamble = 0.000285 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001473 s +UEqn assamble = 0.000919 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000554 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001751 s +YEqn assamble = 0.000631 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000126 s +YEqn correct boundary = 0 s +EEqn Time = 0.000489 s +EEqn assamble = 0.00034 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000149 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 194.01 s ClockTime = 195 s +Courant Number mean: 0.00297164 max: 0.067003 +Time = 0.00161 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 22065 + Current mass in system = 1.45051e-09 + Linear momentum = (1.62518e-11 -8.40746e-09 0) + |Linear momentum| = 8.40748e-09 + Linear kinetic energy = 2.56978e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 405.252, 540.2 + Mass transfer phase change = 2.55634e-10 + D10, D32, Dmax (mu) = 65.7354, 89.0709, 180.816 + Liquid penetration 95% mass (m) = 0.0115108 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.164845, Final residual = 2.98188e-08, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0774894, Final residual = 4.72608e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00561194, Final residual = 4.73998e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000636996, Final residual = 7.18588e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0010601, Final residual = 1.18647e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00105966, Final residual = 1.19093e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00171101, Final residual = 1.22921e-07, No Iterations 1 +min/max(T) = 806.181, 2738.63 +GAMG: Solving for p, Initial residual = 0.0582851, Final residual = 0.000963148, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.01386e-05, global = 6.68045e-05, cumulative = 0.0057702 +GAMG: Solving for p, Initial residual = 0.00102366, Final residual = 9.66489e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.73736e-05, global = 6.73709e-05, cumulative = 0.00583757 +smoothSolver: Solving for epsilon, Initial residual = 0.00358278, Final residual = 5.91385e-10, No Iterations 2 +smoothSolver: Solving for k, Initial residual = 0.00283436, Final residual = 7.82945e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.097744 s +other Time = 1e-06 s +rho Equations = 0.000189 s +U Equations = 0.001433 s +Y Equations = 0.00246636 s +E Equations = 0.0005 s +p Equations = 0.002132 s +calculate parcels = 132.654 s +chemistry correctThermo = 0.002008 s +turbulence correct = 0.000903 s +combustion correct(in Y) = 0.0879086 s +percentage of chemistry = 89.9376 % +percentage of rho/U/Y/E = 4.69426 % +========Time details of each equation======= +rhoEqn Time = 0.000313 s +rhoEqn assamble = 0.000245 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001431 s +UEqn assamble = 0.000873 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000558 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001805 s +YEqn assamble = 0.000647 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000189 s +YEqn correct boundary = 0 s +EEqn Time = 0.000377 s +EEqn assamble = 0.000281 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 194.49 s ClockTime = 195 s +Courant Number mean: 0.00325184 max: 0.0837063 +Time = 0.0016125 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21986 + Current mass in system = 1.44463e-09 + Linear momentum = (1.92975e-11 -8.32906e-09 0) + |Linear momentum| = 8.32908e-09 + Linear kinetic energy = 2.53431e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 405.395, 540.2 + Mass transfer phase change = 2.61516e-10 + D10, D32, Dmax (mu) = 66.9077, 89.1484, 180.461 + Liquid penetration 95% mass (m) = 0.011524 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.188669, Final residual = 4.99844e-08, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.102845, Final residual = 1.23876e-08, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00578507, Final residual = 7.10825e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000804623, Final residual = 1.53535e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0012456, Final residual = 2.20928e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00124441, Final residual = 2.21517e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00208867, Final residual = 2.13487e-07, No Iterations 1 +min/max(T) = 806.162, 2723.54 +GAMG: Solving for p, Initial residual = 0.0827305, Final residual = 0.00142409, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 7.36266e-05, global = 6.7073e-05, cumulative = 0.00590465 +GAMG: Solving for p, Initial residual = 0.0015248, Final residual = 8.67975e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 6.77865e-05, global = 6.77827e-05, cumulative = 0.00597243 +smoothSolver: Solving for epsilon, Initial residual = 0.00552652, Final residual = 2.04482e-09, No Iterations 2 +smoothSolver: Solving for k, Initial residual = 0.0045447, Final residual = 2.43849e-09, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.10562 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001263 s +Y Equations = 0.00273781 s +E Equations = 0.000662 s +p Equations = 0.002813 s +calculate parcels = 133.004 s +chemistry correctThermo = 0.002834 s +turbulence correct = 0.001163 s +combustion correct(in Y) = 0.0937642 s +percentage of chemistry = 88.775 % +percentage of rho/U/Y/E = 4.58228 % +========Time details of each equation======= +rhoEqn Time = 0.000338 s +rhoEqn assamble = 0.000266 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001262 s +UEqn assamble = 0.000749 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000513 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002087 s +YEqn assamble = 0.000715 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000207 s +YEqn correct boundary = 0 s +EEqn Time = 0.000467 s +EEqn assamble = 0.000347 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00012 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 194.95 s ClockTime = 195 s +Courant Number mean: 0.00351252 max: 0.142323 +Time = 0.001615 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21974 + Current mass in system = 1.44158e-09 + Linear momentum = (1.62544e-11 -8.23054e-09 0) + |Linear momentum| = 8.23056e-09 + Linear kinetic energy = 2.4884e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 405.564, 540.2 + Mass transfer phase change = 2.64568e-10 + D10, D32, Dmax (mu) = 66.5102, 88.8551, 180.209 + Liquid penetration 95% mass (m) = 0.0115369 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.184586, Final residual = 4.6855e-08, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.114822, Final residual = 1.48631e-08, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00323667, Final residual = 5.36471e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000997786, Final residual = 1.80815e-07, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00119162, Final residual = 2.39516e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00119018, Final residual = 2.401e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00203781, Final residual = 2.3947e-07, No Iterations 1 +min/max(T) = 806.144, 2714.4 +GAMG: Solving for p, Initial residual = 0.0939712, Final residual = 0.00129772, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.01281e-05, global = 3.5077e-05, cumulative = 0.00600751 +GAMG: Solving for p, Initial residual = 0.00185365, Final residual = 2.78393e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.51776e-05, global = 3.51769e-05, cumulative = 0.00604268 +smoothSolver: Solving for epsilon, Initial residual = 0.00355464, Final residual = 5.81266e-10, No Iterations 2 +smoothSolver: Solving for k, Initial residual = 0.00323009, Final residual = 8.51091e-10, No Iterations 2 +========Time Spent in diffenet parts======== +loop Time = 0.084374 s +other Time = 0 s +rho Equations = 0.000171 s +U Equations = 0.001163 s +Y Equations = 0.00242276 s +E Equations = 0.000625 s +p Equations = 0.003418 s +calculate parcels = 133.272 s +chemistry correctThermo = 0.002843 s +turbulence correct = 0.001351 s +combustion correct(in Y) = 0.0721662 s +percentage of chemistry = 85.5314 % +percentage of rho/U/Y/E = 5.19326 % +========Time details of each equation======= +rhoEqn Time = 0.000371 s +rhoEqn assamble = 0.000293 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001163 s +UEqn assamble = 0.000732 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000431 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001811 s +YEqn assamble = 0.000634 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000206 s +YEqn correct boundary = 0 s +EEqn Time = 0.000466 s +EEqn assamble = 0.000351 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 195.3 s ClockTime = 196 s +Courant Number mean: 0.00346249 max: 0.0944607 +Time = 0.0016175 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21973 + Current mass in system = 1.43939e-09 + Linear momentum = (4.30516e-12 -8.14496e-09 0) + |Linear momentum| = 8.14496e-09 + Linear kinetic energy = 2.44834e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 405.682, 540.2 + Mass transfer phase change = 2.66749e-10 + D10, D32, Dmax (mu) = 66.187, 88.5903, 180.052 + Liquid penetration 95% mass (m) = 0.0115492 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.184501, Final residual = 2.90398e-08, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.109205, Final residual = 9.47109e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00173648, Final residual = 1.808e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000870572, Final residual = 8.57584e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000973336, Final residual = 1.14148e-07, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000972392, Final residual = 1.1449e-07, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00161358, Final residual = 1.37072e-07, No Iterations 1 +min/max(T) = 806.127, 2713.41 +GAMG: Solving for p, Initial residual = 0.0985307, Final residual = 0.0091286, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.80701e-05, global = 3.57938e-05, cumulative = 0.00607848 +GAMG: Solving for p, Initial residual = 0.00891938, Final residual = 3.05237e-07, No Iterations 6 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.51379e-05, global = 2.51372e-05, cumulative = 0.00610362 +smoothSolver: Solving for epsilon, Initial residual = 0.00209405, Final residual = 4.14135e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00190857, Final residual = 4.85084e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095649 s +other Time = 0 s +rho Equations = 0.000183 s +U Equations = 0.001294 s +Y Equations = 0.00244943 s +E Equations = 0.000626 s +p Equations = 0.002825 s +calculate parcels = 133.634 s +chemistry correctThermo = 0.002846 s +turbulence correct = 0.000957 s +combustion correct(in Y) = 0.0842626 s +percentage of chemistry = 88.0956 % +percentage of rho/U/Y/E = 4.75951 % +========Time details of each equation======= +rhoEqn Time = 0.000331 s +rhoEqn assamble = 0.00026 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001293 s +UEqn assamble = 0.00078 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000513 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001802 s +YEqn assamble = 0.00063 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000183 s +YEqn correct boundary = 0 s +EEqn Time = 0.000455 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 195.76 s ClockTime = 196 s +Courant Number mean: 0.00324681 max: 0.0378716 +Time = 0.00162 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21973 + Current mass in system = 1.43754e-09 + Linear momentum = (-2.97935e-12 -8.09611e-09 0) + |Linear momentum| = 8.09611e-09 + Linear kinetic energy = 2.42583e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 405.967, 540.2 + Mass transfer phase change = 2.68603e-10 + D10, D32, Dmax (mu) = 65.9726, 88.4252, 179.862 + Liquid penetration 95% mass (m) = 0.0115614 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.158306, Final residual = 1.70133e-08, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.10917, Final residual = 7.3758e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00127548, Final residual = 9.41958e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000598322, Final residual = 4.86632e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000705526, Final residual = 5.90221e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000704987, Final residual = 5.91582e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00123966, Final residual = 9.97094e-08, No Iterations 1 +min/max(T) = 806.11, 2716.26 +GAMG: Solving for p, Initial residual = 0.0938152, Final residual = 0.00923243, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 5.2045e-05, global = 2.91555e-05, cumulative = 0.00613277 +GAMG: Solving for p, Initial residual = 0.00892289, Final residual = 2.05448e-07, No Iterations 6 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.13743e-05, global = 2.13738e-05, cumulative = 0.00615414 +smoothSolver: Solving for epsilon, Initial residual = 0.00130349, Final residual = 1.97681e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00133047, Final residual = 2.5365e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100163 s +other Time = 1e-06 s +rho Equations = 0.000184 s +U Equations = 0.001289 s +Y Equations = 0.00258202 s +E Equations = 0.000638 s +p Equations = 0.002962 s +calculate parcels = 133.963 s +chemistry correctThermo = 0.003018 s +turbulence correct = 0.001135 s +combustion correct(in Y) = 0.088148 s +percentage of chemistry = 88.0045 % +percentage of rho/U/Y/E = 4.68539 % +========Time details of each equation======= +rhoEqn Time = 0.000339 s +rhoEqn assamble = 0.000264 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001289 s +UEqn assamble = 0.000784 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000505 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001888 s +YEqn assamble = 0.000672 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000199 s +YEqn correct boundary = 0 s +EEqn Time = 0.000479 s +EEqn assamble = 0.000354 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000125 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 196.19 s ClockTime = 197 s +Courant Number mean: 0.00296378 max: 0.0220254 +Time = 0.0016225 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21973 + Current mass in system = 1.43594e-09 + Linear momentum = (-5.00494e-12 -8.07184e-09 0) + |Linear momentum| = 8.07184e-09 + Linear kinetic energy = 2.41505e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 406.316, 540.2 + Mass transfer phase change = 2.70201e-10 + D10, D32, Dmax (mu) = 65.8305, 88.3447, 179.611 + Liquid penetration 95% mass (m) = 0.011574 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.152824, Final residual = 1.23051e-08, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.113544, Final residual = 5.82395e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00118952, Final residual = 7.72489e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000503232, Final residual = 4.65655e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000586806, Final residual = 5.02837e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000586343, Final residual = 5.04157e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0011573, Final residual = 7.95359e-08, No Iterations 1 +min/max(T) = 806.093, 2721.29 +GAMG: Solving for p, Initial residual = 0.0863409, Final residual = 0.00848415, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.67236e-05, global = 2.32534e-05, cumulative = 0.0061774 +GAMG: Solving for p, Initial residual = 0.00794721, Final residual = 5.8389e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.84194e-05, global = 1.84177e-05, cumulative = 0.00619582 +smoothSolver: Solving for epsilon, Initial residual = 0.000999422, Final residual = 1.44382e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00117796, Final residual = 2.0885e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.090649 s +other Time = 0 s +rho Equations = 0.000151 s +U Equations = 0.001083 s +Y Equations = 0.00233971 s +E Equations = 0.000599 s +p Equations = 0.002793 s +calculate parcels = 134.313 s +chemistry correctThermo = 0.00288 s +turbulence correct = 0.000988 s +combustion correct(in Y) = 0.0796293 s +percentage of chemistry = 87.8435 % +percentage of rho/U/Y/E = 4.60315 % +========Time details of each equation======= +rhoEqn Time = 0.000302 s +rhoEqn assamble = 0.00024 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001081 s +UEqn assamble = 0.000658 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000423 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.0018 s +YEqn assamble = 0.000622 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000233 s +YEqn correct boundary = 0 s +EEqn Time = 0.000445 s +EEqn assamble = 0.00033 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 196.63 s ClockTime = 197 s +Courant Number mean: 0.00267691 max: 0.0169526 +Time = 0.001625 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21973 + Current mass in system = 1.43446e-09 + Linear momentum = (-4.79849e-12 -8.05338e-09 0) + |Linear momentum| = 8.05338e-09 + Linear kinetic energy = 2.40679e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 406.697, 540.2 + Mass transfer phase change = 2.71684e-10 + D10, D32, Dmax (mu) = 65.7188, 88.2905, 180.015 + Liquid penetration 95% mass (m) = 0.0115852 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.226801, Final residual = 1.53729e-08, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.116408, Final residual = 5.12689e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00120593, Final residual = 8.9478e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000537952, Final residual = 5.37598e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000577251, Final residual = 5.80741e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000577043, Final residual = 5.82623e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00126841, Final residual = 8.86523e-08, No Iterations 1 +min/max(T) = 806.078, 2725.25 +GAMG: Solving for p, Initial residual = 0.0752909, Final residual = 0.00697591, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.98185e-05, global = 1.83638e-05, cumulative = 0.00621418 +GAMG: Solving for p, Initial residual = 0.00648228, Final residual = 4.37284e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.70952e-05, global = 1.70935e-05, cumulative = 0.00623127 +smoothSolver: Solving for epsilon, Initial residual = 0.0010473, Final residual = 1.65513e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00125289, Final residual = 2.37845e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102476 s +other Time = 1e-06 s +rho Equations = 0.000158 s +U Equations = 0.001294 s +Y Equations = 0.00261315 s +E Equations = 0.000505 s +p Equations = 0.00228 s +calculate parcels = 134.619 s +chemistry correctThermo = 0.00206 s +turbulence correct = 0.000852 s +combustion correct(in Y) = 0.0924938 s +percentage of chemistry = 90.259 % +percentage of rho/U/Y/E = 4.45973 % +========Time details of each equation======= +rhoEqn Time = 0.00029 s +rhoEqn assamble = 0.000231 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001292 s +UEqn assamble = 0.000634 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000658 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001401 s +YEqn assamble = 0.000585 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -0.000135 s +YEqn correct boundary = 0 s +EEqn Time = 0.000373 s +EEqn assamble = 0.00028 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 197.04 s ClockTime = 198 s +Courant Number mean: 0.00239631 max: 0.0216265 +Time = 0.0016275 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21972 + Current mass in system = 1.4328e-09 + Linear momentum = (-3.64054e-12 -8.03194e-09 0) + |Linear momentum| = 8.03195e-09 + Linear kinetic energy = 2.39701e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 407.102, 540.2 + Mass transfer phase change = 2.73347e-10 + D10, D32, Dmax (mu) = 65.5781, 88.2274, 180.643 + Liquid penetration 95% mass (m) = 0.0115975 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.347672, Final residual = 1.81411e-08, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.114522, Final residual = 4.68094e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00143592, Final residual = 1.24452e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000625359, Final residual = 6.14959e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00067967, Final residual = 7.12391e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000679722, Final residual = 7.15026e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00134716, Final residual = 9.96526e-08, No Iterations 1 +min/max(T) = 806.063, 2727.84 +GAMG: Solving for p, Initial residual = 0.0670874, Final residual = 0.00550825, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.70406e-05, global = 1.74395e-05, cumulative = 0.00624871 +GAMG: Solving for p, Initial residual = 0.00516961, Final residual = 4.46949e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.91636e-05, global = 1.91618e-05, cumulative = 0.00626787 +smoothSolver: Solving for epsilon, Initial residual = 0.00115042, Final residual = 1.9839e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.001307, Final residual = 2.69502e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.089722 s +other Time = 0 s +rho Equations = 0.000178 s +U Equations = 0.001141 s +Y Equations = 0.00251792 s +E Equations = 0.000536 s +p Equations = 0.002321 s +calculate parcels = 134.964 s +chemistry correctThermo = 0.002028 s +turbulence correct = 0.001002 s +combustion correct(in Y) = 0.0798061 s +percentage of chemistry = 88.9482 % +percentage of rho/U/Y/E = 4.87385 % +========Time details of each equation======= +rhoEqn Time = 0.000316 s +rhoEqn assamble = 0.000252 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00114 s +UEqn assamble = 0.000703 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000437 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001953 s +YEqn assamble = 0.000703 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000192 s +YEqn correct boundary = 0 s +EEqn Time = 0.000403 s +EEqn assamble = 0.000305 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 197.47 s ClockTime = 198 s +Courant Number mean: 0.0022851 max: 0.0334108 +Time = 0.00163 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21972 + Current mass in system = 1.43108e-09 + Linear momentum = (-2.05184e-12 -8.00478e-09 0) + |Linear momentum| = 8.00478e-09 + Linear kinetic energy = 2.38446e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 407.52, 540.2 + Mass transfer phase change = 2.75067e-10 + D10, D32, Dmax (mu) = 65.369, 88.124, 181.258 + Liquid penetration 95% mass (m) = 0.0116098 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.331268, Final residual = 1.71369e-08, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.10905, Final residual = 4.29247e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00143952, Final residual = 1.07301e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000653272, Final residual = 6.4454e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000694028, Final residual = 7.21722e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000694203, Final residual = 7.24349e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00140167, Final residual = 9.53585e-08, No Iterations 1 +min/max(T) = 806.049, 2729.66 +GAMG: Solving for p, Initial residual = 0.0706979, Final residual = 0.00557396, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.78378e-05, global = 1.68196e-05, cumulative = 0.00628469 +GAMG: Solving for p, Initial residual = 0.00532852, Final residual = 2.55358e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.98245e-05, global = 1.98236e-05, cumulative = 0.00630452 +smoothSolver: Solving for epsilon, Initial residual = 0.00125567, Final residual = 2.35142e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00137004, Final residual = 3.04783e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.112416 s +other Time = 0 s +rho Equations = 0.000189 s +U Equations = 0.001305 s +Y Equations = 0.00246385 s +E Equations = 0.00062 s +p Equations = 0.002928 s +calculate parcels = 135.241 s +chemistry correctThermo = 0.003114 s +turbulence correct = 0.001103 s +combustion correct(in Y) = 0.100456 s +percentage of chemistry = 89.3611 % +percentage of rho/U/Y/E = 4.07224 % +========Time details of each equation======= +rhoEqn Time = 0.000358 s +rhoEqn assamble = 0.000286 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001305 s +UEqn assamble = 0.000807 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000498 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001814 s +YEqn assamble = 0.000635 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000185 s +YEqn correct boundary = 0 s +EEqn Time = 0.000451 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 197.86 s ClockTime = 198 s +Courant Number mean: 0.00233028 max: 0.0271227 +Time = 0.0016325 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21972 + Current mass in system = 1.42921e-09 + Linear momentum = (5.36105e-14 -7.97094e-09 0) + |Linear momentum| = 7.97094e-09 + Linear kinetic energy = 2.36883e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 407.938, 540.2 + Mass transfer phase change = 2.76936e-10 + D10, D32, Dmax (mu) = 65.116, 87.9846, 181.776 + Liquid penetration 95% mass (m) = 0.011622 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.233244, Final residual = 1.26065e-08, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.100095, Final residual = 3.92285e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00148915, Final residual = 1.00503e-07, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000645183, Final residual = 6.5403e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00069756, Final residual = 7.49692e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000697766, Final residual = 7.52298e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00149105, Final residual = 9.18185e-08, No Iterations 1 +min/max(T) = 806.036, 2731.5 +GAMG: Solving for p, Initial residual = 0.0718969, Final residual = 0.00603401, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.31133e-05, global = 1.78878e-05, cumulative = 0.00632241 +GAMG: Solving for p, Initial residual = 0.00573553, Final residual = 2.37585e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.15474e-05, global = 2.15465e-05, cumulative = 0.00634395 +smoothSolver: Solving for epsilon, Initial residual = 0.00139069, Final residual = 2.61718e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00141204, Final residual = 3.23634e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.107849 s +other Time = 1e-06 s +rho Equations = 0.000212 s +U Equations = 0.001308 s +Y Equations = 0.00253508 s +E Equations = 0.000629 s +p Equations = 0.002672 s +calculate parcels = 135.583 s +chemistry correctThermo = 0.002865 s +turbulence correct = 0.000975 s +combustion correct(in Y) = 0.0964149 s +percentage of chemistry = 89.3981 % +percentage of rho/U/Y/E = 4.34318 % +========Time details of each equation======= +rhoEqn Time = 0.000362 s +rhoEqn assamble = 0.000285 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001307 s +UEqn assamble = 0.000837 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00047 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001946 s +YEqn assamble = 0.00068 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00022 s +YEqn correct boundary = 0 s +EEqn Time = 0.000464 s +EEqn assamble = 0.000338 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000126 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 198.31 s ClockTime = 199 s +Courant Number mean: 0.00236037 max: 0.0250588 +Time = 0.001635 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21972 + Current mass in system = 1.42725e-09 + Linear momentum = (2.32592e-12 -7.93162e-09 0) + |Linear momentum| = 7.93162e-09 + Linear kinetic energy = 2.35074e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 408.346, 540.2 + Mass transfer phase change = 2.78894e-10 + D10, D32, Dmax (mu) = 64.8556, 87.8214, 181.451 + Liquid penetration 95% mass (m) = 0.0116336 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.147949, Final residual = 7.269e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0917109, Final residual = 3.41671e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00147185, Final residual = 9.09778e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000615089, Final residual = 6.50271e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000678577, Final residual = 7.45934e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000678773, Final residual = 7.48519e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00151692, Final residual = 9.07872e-08, No Iterations 1 +min/max(T) = 806.025, 2733.62 +GAMG: Solving for p, Initial residual = 0.0692477, Final residual = 0.00592004, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.4335e-05, global = 1.9061e-05, cumulative = 0.00636301 +GAMG: Solving for p, Initial residual = 0.00559382, Final residual = 8.48044e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.25691e-05, global = 2.25656e-05, cumulative = 0.00638558 +smoothSolver: Solving for epsilon, Initial residual = 0.0014244, Final residual = 2.61807e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0013897, Final residual = 3.1263e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.104695 s +other Time = 0 s +rho Equations = 0.000183 s +U Equations = 0.001259 s +Y Equations = 0.00210446 s +E Equations = 0.000489 s +p Equations = 0.002064 s +calculate parcels = 135.91 s +chemistry correctThermo = 0.005006 s +turbulence correct = 0.000946 s +combustion correct(in Y) = 0.0924225 s +percentage of chemistry = 88.2779 % +percentage of rho/U/Y/E = 3.85449 % +========Time details of each equation======= +rhoEqn Time = 0.000308 s +rhoEqn assamble = 0.000241 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001258 s +UEqn assamble = 0.000752 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000506 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001468 s +YEqn assamble = 0.000537 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000108 s +YEqn correct boundary = 0 s +EEqn Time = 0.00037 s +EEqn assamble = 0.000274 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 198.74 s ClockTime = 199 s +Courant Number mean: 0.00230413 max: 0.0246063 +Time = 0.0016375 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21972 + Current mass in system = 1.42527e-09 + Linear momentum = (4.33059e-12 -7.89032e-09 0) + |Linear momentum| = 7.89032e-09 + Linear kinetic energy = 2.33188e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 408.742, 540.2 + Mass transfer phase change = 2.80878e-10 + D10, D32, Dmax (mu) = 64.6123, 87.6517, 181.141 + Liquid penetration 95% mass (m) = 0.011646 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.101279, Final residual = 5.1085e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0855916, Final residual = 2.91054e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00143019, Final residual = 8.70679e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000574173, Final residual = 6.01545e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00064021, Final residual = 6.9228e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000640336, Final residual = 6.94695e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00147517, Final residual = 8.77165e-08, No Iterations 1 +min/max(T) = 806.014, 2735.85 +GAMG: Solving for p, Initial residual = 0.0634471, Final residual = 0.00504866, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 4.17735e-05, global = 2.00017e-05, cumulative = 0.00640558 +GAMG: Solving for p, Initial residual = 0.00479456, Final residual = 6.07296e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.28671e-05, global = 2.28646e-05, cumulative = 0.00642844 +smoothSolver: Solving for epsilon, Initial residual = 0.00136555, Final residual = 2.45282e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00130081, Final residual = 2.84865e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.11014 s +other Time = 0 s +rho Equations = 0.0002 s +U Equations = 0.00126 s +Y Equations = 0.00251886 s +E Equations = 0.000602 s +p Equations = 0.002377 s +calculate parcels = 136.257 s +chemistry correctThermo = 0.002861 s +turbulence correct = 0.00097 s +combustion correct(in Y) = 0.0991381 s +percentage of chemistry = 90.011 % +percentage of rho/U/Y/E = 4.15912 % +========Time details of each equation======= +rhoEqn Time = 0.000339 s +rhoEqn assamble = 0.000258 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001258 s +UEqn assamble = 0.000735 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000523 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001859 s +YEqn assamble = 0.000651 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000185 s +YEqn correct boundary = 0 s +EEqn Time = 0.000445 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 199.2 s ClockTime = 200 s +Courant Number mean: 0.00214676 max: 0.024368 +Time = 0.00164 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21972 + Current mass in system = 1.42331e-09 + Linear momentum = (5.95392e-12 -7.8512e-09 0) + |Linear momentum| = 7.8512e-09 + Linear kinetic energy = 2.3142e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 409.13, 540.2 + Mass transfer phase change = 2.82837e-10 + D10, D32, Dmax (mu) = 64.3973, 87.4907, 180.847 + Liquid penetration 95% mass (m) = 0.0116573 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.126692, Final residual = 7.67215e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0822661, Final residual = 2.57933e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0013734, Final residual = 8.30458e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000531059, Final residual = 5.32609e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00059493, Final residual = 6.17746e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00059505, Final residual = 6.19944e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00137447, Final residual = 8.15352e-08, No Iterations 1 +min/max(T) = 806.006, 2737.86 +GAMG: Solving for p, Initial residual = 0.0541825, Final residual = 0.00404956, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.82435e-05, global = 2.06062e-05, cumulative = 0.00644905 +GAMG: Solving for p, Initial residual = 0.00386006, Final residual = 6.23599e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.25869e-05, global = 2.25844e-05, cumulative = 0.00647164 +smoothSolver: Solving for epsilon, Initial residual = 0.00125951, Final residual = 2.2284e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00117964, Final residual = 2.5146e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.1109 s +other Time = 1e-06 s +rho Equations = 0.000176 s +U Equations = 0.001248 s +Y Equations = 0.00287454 s +E Equations = 0.000635 s +p Equations = 0.002582 s +calculate parcels = 136.64 s +chemistry correctThermo = 0.002862 s +turbulence correct = 0.001012 s +combustion correct(in Y) = 0.0993065 s +percentage of chemistry = 89.546 % +percentage of rho/U/Y/E = 4.44864 % +========Time details of each equation======= +rhoEqn Time = 0.00033 s +rhoEqn assamble = 0.000261 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001248 s +UEqn assamble = 0.000758 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00049 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002143 s +YEqn assamble = 0.000787 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000212 s +YEqn correct boundary = 0 s +EEqn Time = 0.000465 s +EEqn assamble = 0.000347 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 199.69 s ClockTime = 200 s +Courant Number mean: 0.00190809 max: 0.0241918 +Time = 0.0016425 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21972 + Current mass in system = 1.4214e-09 + Linear momentum = (7.29059e-12 -7.81644e-09 0) + |Linear momentum| = 7.81645e-09 + Linear kinetic energy = 2.29867e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 409.515, 540.2 + Mass transfer phase change = 2.84743e-10 + D10, D32, Dmax (mu) = 64.2155, 87.3468, 180.567 + Liquid penetration 95% mass (m) = 0.0116685 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.217892, Final residual = 1.13336e-08, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0834808, Final residual = 2.60189e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00131057, Final residual = 7.94031e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000488846, Final residual = 4.67967e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000545771, Final residual = 5.40472e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000545879, Final residual = 5.42407e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00122528, Final residual = 7.35959e-08, No Iterations 1 +min/max(T) = 805.998, 2739.38 +GAMG: Solving for p, Initial residual = 0.0450717, Final residual = 0.00314138, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.46318e-05, global = 2.08581e-05, cumulative = 0.00649249 +GAMG: Solving for p, Initial residual = 0.00300003, Final residual = 4.89666e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.19639e-05, global = 2.19619e-05, cumulative = 0.00651446 +smoothSolver: Solving for epsilon, Initial residual = 0.00115519, Final residual = 2.02421e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00108449, Final residual = 2.24851e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.077728 s +other Time = 0 s +rho Equations = 0.000173 s +U Equations = 0.001174 s +Y Equations = 0.00212699 s +E Equations = 0.000481 s +p Equations = 0.001947 s +calculate parcels = 136.927 s +chemistry correctThermo = 0.001993 s +turbulence correct = 0.000938 s +combustion correct(in Y) = 0.0687 s +percentage of chemistry = 88.3851 % +percentage of rho/U/Y/E = 5.08824 % +========Time details of each equation======= +rhoEqn Time = 0.000294 s +rhoEqn assamble = 0.000232 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001174 s +UEqn assamble = 0.000741 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000433 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001529 s +YEqn assamble = 0.00055 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000111 s +YEqn correct boundary = 0 s +EEqn Time = 0.00036 s +EEqn assamble = 0.000269 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 200.06 s ClockTime = 201 s +Courant Number mean: 0.00163308 max: 0.0240721 +Time = 0.001645 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21972 + Current mass in system = 1.41956e-09 + Linear momentum = (8.47584e-12 -7.78645e-09 0) + |Linear momentum| = 7.78645e-09 + Linear kinetic energy = 2.2854e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 409.903, 540.2 + Mass transfer phase change = 2.8658e-10 + D10, D32, Dmax (mu) = 64.0642, 87.2222, 180.294 + Liquid penetration 95% mass (m) = 0.0116803 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.3175, Final residual = 1.34066e-08, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0872618, Final residual = 2.63905e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00124621, Final residual = 7.6474e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000453556, Final residual = 4.2263e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000501363, Final residual = 4.77546e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000501419, Final residual = 4.7921e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00106899, Final residual = 6.68423e-08, No Iterations 1 +min/max(T) = 805.992, 2740.29 +GAMG: Solving for p, Initial residual = 0.0403051, Final residual = 0.0025732, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.19088e-05, global = 2.08149e-05, cumulative = 0.00653527 +GAMG: Solving for p, Initial residual = 0.00246308, Final residual = 2.44253e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.11819e-05, global = 2.1181e-05, cumulative = 0.00655645 +smoothSolver: Solving for epsilon, Initial residual = 0.00107913, Final residual = 1.85988e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00103928, Final residual = 2.06346e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.093753 s +other Time = 1e-06 s +rho Equations = 0.00016 s +U Equations = 0.001119 s +Y Equations = 0.00251891 s +E Equations = 0.000619 s +p Equations = 0.002907 s +calculate parcels = 137.257 s +chemistry correctThermo = 0.002843 s +turbulence correct = 0.001245 s +combustion correct(in Y) = 0.0821331 s +percentage of chemistry = 87.6058 % +percentage of rho/U/Y/E = 4.71122 % +========Time details of each equation======= +rhoEqn Time = 0.000342 s +rhoEqn assamble = 0.000271 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001118 s +UEqn assamble = 0.000692 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000426 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001958 s +YEqn assamble = 0.000663 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000273 s +YEqn correct boundary = 0 s +EEqn Time = 0.000459 s +EEqn assamble = 0.00034 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000119 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 200.48 s ClockTime = 201 s +Courant Number mean: 0.00143454 max: 0.0238161 +Time = 0.0016475 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21972 + Current mass in system = 1.4178e-09 + Linear momentum = (9.62474e-12 -7.76087e-09 0) + |Linear momentum| = 7.76088e-09 + Linear kinetic energy = 2.27421e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 410.295, 540.2 + Mass transfer phase change = 2.88344e-10 + D10, D32, Dmax (mu) = 63.9351, 87.1161, 180.026 + Liquid penetration 95% mass (m) = 0.0116912 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.298878, Final residual = 1.06519e-08, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0917708, Final residual = 2.63482e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00117953, Final residual = 7.30628e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000435944, Final residual = 3.96365e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000475575, Final residual = 4.43352e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000475509, Final residual = 4.44805e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000964934, Final residual = 6.26169e-08, No Iterations 1 +min/max(T) = 805.989, 2740.65 +GAMG: Solving for p, Initial residual = 0.0374459, Final residual = 0.00264309, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.16149e-05, global = 2.05225e-05, cumulative = 0.00657697 +GAMG: Solving for p, Initial residual = 0.00254057, Final residual = 2.07375e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.03313e-05, global = 2.03306e-05, cumulative = 0.0065973 +smoothSolver: Solving for epsilon, Initial residual = 0.00101226, Final residual = 1.70038e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00104019, Final residual = 1.97502e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.109446 s +other Time = 0 s +rho Equations = 0.000206 s +U Equations = 0.001233 s +Y Equations = 0.00240683 s +E Equations = 0.000595 s +p Equations = 0.002437 s +calculate parcels = 137.615 s +chemistry correctThermo = 0.002884 s +turbulence correct = 0.001003 s +combustion correct(in Y) = 0.0984292 s +percentage of chemistry = 89.934 % +percentage of rho/U/Y/E = 4.05755 % +========Time details of each equation======= +rhoEqn Time = 0.000352 s +rhoEqn assamble = 0.000279 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001232 s +UEqn assamble = 0.000734 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000498 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001762 s +YEqn assamble = 0.000621 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000175 s +YEqn correct boundary = 0 s +EEqn Time = 0.000438 s +EEqn assamble = 0.000325 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 200.95 s ClockTime = 201 s +Courant Number mean: 0.0014027 max: 0.0233815 +Time = 0.00165 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21972 + Current mass in system = 1.41611e-09 + Linear momentum = (1.07424e-11 -7.73898e-09 0) + |Linear momentum| = 7.73899e-09 + Linear kinetic energy = 2.26474e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 410.688, 540.2 + Mass transfer phase change = 2.90034e-10 + D10, D32, Dmax (mu) = 63.8195, 87.0272, 179.762 + Liquid penetration 95% mass (m) = 0.0117025 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.210097, Final residual = 7.12882e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0974763, Final residual = 2.74752e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00112296, Final residual = 7.1509e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000442603, Final residual = 3.90851e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000475843, Final residual = 4.37439e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00047567, Final residual = 4.3872e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00091937, Final residual = 6.16494e-08, No Iterations 1 +min/max(T) = 805.987, 2740.67 +GAMG: Solving for p, Initial residual = 0.038538, Final residual = 0.00295677, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.22091e-05, global = 1.99794e-05, cumulative = 0.00661728 +GAMG: Solving for p, Initial residual = 0.00284116, Final residual = 3.69469e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.94758e-05, global = 1.94745e-05, cumulative = 0.00663676 +smoothSolver: Solving for epsilon, Initial residual = 0.000980633, Final residual = 1.56318e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00104822, Final residual = 1.8874e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.114619 s +other Time = 1e-06 s +rho Equations = 0.000238 s +U Equations = 0.001859 s +Y Equations = 0.00268244 s +E Equations = 0.000612 s +p Equations = 0.002548 s +calculate parcels = 137.95 s +chemistry correctThermo = 0.002883 s +turbulence correct = 0.001027 s +combustion correct(in Y) = 0.102526 s +percentage of chemistry = 89.449 % +percentage of rho/U/Y/E = 4.7038 % +========Time details of each equation======= +rhoEqn Time = 0.00039 s +rhoEqn assamble = 0.000299 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001858 s +UEqn assamble = 0.00109 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000768 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001652 s +YEqn assamble = 0.000653 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -8e-06 s +YEqn correct boundary = 0 s +EEqn Time = 0.000452 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 201.4 s ClockTime = 202 s +Courant Number mean: 0.00141107 max: 0.0224081 +Time = 0.0016525 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21970 + Current mass in system = 1.41449e-09 + Linear momentum = (1.17941e-11 -7.72002e-09 0) + |Linear momentum| = 7.72003e-09 + Linear kinetic energy = 2.25664e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 411.08, 540.2 + Mass transfer phase change = 2.91654e-10 + D10, D32, Dmax (mu) = 63.8549, 86.9572, 179.504 + Liquid penetration 95% mass (m) = 0.0117138 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.136057, Final residual = 4.30775e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.10456, Final residual = 2.91283e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00108359, Final residual = 7.15756e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000466159, Final residual = 3.95625e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000494039, Final residual = 4.43354e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000493804, Final residual = 4.44692e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000933, Final residual = 6.27426e-08, No Iterations 1 +min/max(T) = 805.988, 2740.63 +GAMG: Solving for p, Initial residual = 0.0390362, Final residual = 0.00306414, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.20245e-05, global = 1.92068e-05, cumulative = 0.00665597 +GAMG: Solving for p, Initial residual = 0.00294354, Final residual = 4.50216e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.8676e-05, global = 1.86745e-05, cumulative = 0.00667464 +smoothSolver: Solving for epsilon, Initial residual = 0.000971069, Final residual = 1.42472e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00105661, Final residual = 1.79188e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.099388 s +other Time = 0 s +rho Equations = 0.000182 s +U Equations = 0.001217 s +Y Equations = 0.00213535 s +E Equations = 0.000518 s +p Equations = 0.001969 s +calculate parcels = 138.312 s +chemistry correctThermo = 0.002048 s +turbulence correct = 0.000847 s +combustion correct(in Y) = 0.0902766 s +percentage of chemistry = 90.8325 % +percentage of rho/U/Y/E = 4.07731 % +========Time details of each equation======= +rhoEqn Time = 0.000303 s +rhoEqn assamble = 0.000239 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001215 s +UEqn assamble = 0.000717 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000498 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001505 s +YEqn assamble = 0.000539 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000106 s +YEqn correct boundary = 0 s +EEqn Time = 0.000379 s +EEqn assamble = 0.00028 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 201.86 s ClockTime = 202 s +Courant Number mean: 0.00138286 max: 0.0209297 +Time = 0.001655 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21970 + Current mass in system = 1.41294e-09 + Linear momentum = (1.27482e-11 -7.70335e-09 0) + |Linear momentum| = 7.70336e-09 + Linear kinetic energy = 2.2496e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 411.466, 540.2 + Mass transfer phase change = 2.932e-10 + D10, D32, Dmax (mu) = 63.7468, 86.8968, 179.253 + Liquid penetration 95% mass (m) = 0.0117258 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0982581, Final residual = 3.31718e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.112541, Final residual = 3.08415e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00104964, Final residual = 7.20788e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000492726, Final residual = 4.00681e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000518995, Final residual = 4.49965e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000518746, Final residual = 4.51332e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000958637, Final residual = 6.4272e-08, No Iterations 1 +min/max(T) = 805.991, 2740.8 +GAMG: Solving for p, Initial residual = 0.0370567, Final residual = 0.00285275, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.0443e-05, global = 1.81075e-05, cumulative = 0.00669275 +GAMG: Solving for p, Initial residual = 0.00273221, Final residual = 3.87301e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.78203e-05, global = 1.7819e-05, cumulative = 0.00671057 +smoothSolver: Solving for epsilon, Initial residual = 0.000961189, Final residual = 1.32113e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00105305, Final residual = 1.71559e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097656 s +other Time = 1e-06 s +rho Equations = 0.000227 s +U Equations = 0.001842 s +Y Equations = 0.00228013 s +E Equations = 0.000507 s +p Equations = 0.002062 s +calculate parcels = 138.604 s +chemistry correctThermo = 0.002015 s +turbulence correct = 0.000903 s +combustion correct(in Y) = 0.0875689 s +percentage of chemistry = 89.6708 % +percentage of rho/U/Y/E = 4.97269 % +========Time details of each equation======= +rhoEqn Time = 0.000366 s +rhoEqn assamble = 0.000283 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00184 s +UEqn assamble = 0.000969 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000871 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001702 s +YEqn assamble = 0.000554 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000143 s +YEqn correct boundary = 0 s +EEqn Time = 0.000383 s +EEqn assamble = 0.000291 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 202.25 s ClockTime = 203 s +Courant Number mean: 0.00130747 max: 0.0191347 +Time = 0.0016575 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21970 + Current mass in system = 1.41146e-09 + Linear momentum = (1.35849e-11 -7.68834e-09 0) + |Linear momentum| = 7.68835e-09 + Linear kinetic energy = 2.24333e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 411.79, 540.2 + Mass transfer phase change = 2.94684e-10 + D10, D32, Dmax (mu) = 63.6469, 86.8475, 179.012 + Liquid penetration 95% mass (m) = 0.0117368 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.12197, Final residual = 4.51059e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.120802, Final residual = 3.21322e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00102677, Final residual = 7.29301e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000519416, Final residual = 4.10903e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000543739, Final residual = 4.62075e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000543513, Final residual = 4.63477e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000963915, Final residual = 6.58469e-08, No Iterations 1 +min/max(T) = 805.996, 2741.33 +GAMG: Solving for p, Initial residual = 0.0338234, Final residual = 0.00239191, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.79048e-05, global = 1.69352e-05, cumulative = 0.0067275 +GAMG: Solving for p, Initial residual = 0.00227935, Final residual = 2.96963e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.71033e-05, global = 1.71023e-05, cumulative = 0.0067446 +smoothSolver: Solving for epsilon, Initial residual = 0.000952295, Final residual = 1.27115e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00105376, Final residual = 1.68661e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094525 s +other Time = 0 s +rho Equations = 0.000171 s +U Equations = 0.001014 s +Y Equations = 0.00242887 s +E Equations = 0.000605 s +p Equations = 0.002038 s +calculate parcels = 138.871 s +chemistry correctThermo = 0.002885 s +turbulence correct = 0.000858 s +combustion correct(in Y) = 0.0843301 s +percentage of chemistry = 89.2146 % +percentage of rho/U/Y/E = 4.46323 % +========Time details of each equation======= +rhoEqn Time = 0.000296 s +rhoEqn assamble = 0.000234 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001012 s +UEqn assamble = 0.000604 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000408 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001877 s +YEqn assamble = 0.000629 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000248 s +YEqn correct boundary = 0 s +EEqn Time = 0.000449 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 202.61 s ClockTime = 203 s +Courant Number mean: 0.00122859 max: 0.0172375 +Time = 0.00166 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21970 + Current mass in system = 1.41002e-09 + Linear momentum = (1.43216e-11 -7.67451e-09 0) + |Linear momentum| = 7.67453e-09 + Linear kinetic energy = 2.23762e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 412.024, 540.2 + Mass transfer phase change = 2.96119e-10 + D10, D32, Dmax (mu) = 63.5553, 86.8066, 178.781 + Liquid penetration 95% mass (m) = 0.0117477 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.182043, Final residual = 6.26408e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.12666, Final residual = 3.31795e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00101667, Final residual = 7.58019e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000546541, Final residual = 4.31387e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000570865, Final residual = 4.86567e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000570676, Final residual = 4.88084e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000963431, Final residual = 6.81473e-08, No Iterations 1 +min/max(T) = 806.004, 2742.3 +GAMG: Solving for p, Initial residual = 0.0305198, Final residual = 0.00180063, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.47168e-05, global = 1.57861e-05, cumulative = 0.00676039 +GAMG: Solving for p, Initial residual = 0.00171578, Final residual = 2.11489e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.65362e-05, global = 1.65354e-05, cumulative = 0.00677693 +smoothSolver: Solving for epsilon, Initial residual = 0.0009535, Final residual = 1.2551e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00104806, Final residual = 1.6777e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.110087 s +other Time = 0 s +rho Equations = 0.000186 s +U Equations = 0.001358 s +Y Equations = 0.00243175 s +E Equations = 0.000591 s +p Equations = 0.002464 s +calculate parcels = 139.207 s +chemistry correctThermo = 0.002851 s +turbulence correct = 0.001037 s +combustion correct(in Y) = 0.0989502 s +percentage of chemistry = 89.8837 % +percentage of rho/U/Y/E = 4.14831 % +========Time details of each equation======= +rhoEqn Time = 0.000332 s +rhoEqn assamble = 0.000261 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001358 s +UEqn assamble = 0.000842 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000516 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001778 s +YEqn assamble = 0.000639 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000181 s +YEqn correct boundary = 0 s +EEqn Time = 0.00044 s +EEqn assamble = 0.000327 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 203.06 s ClockTime = 204 s +Courant Number mean: 0.00120274 max: 0.0154854 +Time = 0.0016625 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21970 + Current mass in system = 1.40862e-09 + Linear momentum = (1.49671e-11 -7.66142e-09 0) + |Linear momentum| = 7.66143e-09 + Linear kinetic energy = 2.23225e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 412.254, 540.2 + Mass transfer phase change = 2.97523e-10 + D10, D32, Dmax (mu) = 63.47, 86.7712, 179.15 + Liquid penetration 95% mass (m) = 0.0117581 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.215558, Final residual = 7.33639e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.127798, Final residual = 3.38786e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00101648, Final residual = 7.74871e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000578265, Final residual = 4.547e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000604592, Final residual = 5.16732e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000604525, Final residual = 5.18319e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000965769, Final residual = 7.03512e-08, No Iterations 1 +min/max(T) = 806.014, 2743.68 +GAMG: Solving for p, Initial residual = 0.0277292, Final residual = 0.00133926, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.21041e-05, global = 1.4865e-05, cumulative = 0.00679179 +GAMG: Solving for p, Initial residual = 0.00127748, Final residual = 1.61921e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.61823e-05, global = 1.61816e-05, cumulative = 0.00680797 +smoothSolver: Solving for epsilon, Initial residual = 0.000952093, Final residual = 1.25533e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0010347, Final residual = 1.68672e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.10497 s +other Time = 0 s +rho Equations = 0.000153 s +U Equations = 0.000984 s +Y Equations = 0.00268565 s +E Equations = 0.000635 s +p Equations = 0.00257 s +calculate parcels = 139.566 s +chemistry correctThermo = 0.002978 s +turbulence correct = 0.001045 s +combustion correct(in Y) = 0.0937374 s +percentage of chemistry = 89.2992 % +percentage of rho/U/Y/E = 4.24659 % +========Time details of each equation======= +rhoEqn Time = 0.000309 s +rhoEqn assamble = 0.000243 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000982 s +UEqn assamble = 0.000568 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000414 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002138 s +YEqn assamble = 0.000784 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.0003 s +YEqn correct boundary = 0 s +EEqn Time = 0.000463 s +EEqn assamble = 0.000348 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 203.52 s ClockTime = 204 s +Courant Number mean: 0.0012496 max: 0.0146459 +Time = 0.001665 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21970 + Current mass in system = 1.40723e-09 + Linear momentum = (1.55422e-11 -7.64867e-09 0) + |Linear momentum| = 7.64868e-09 + Linear kinetic energy = 2.22706e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 412.483, 540.2 + Mass transfer phase change = 2.98914e-10 + D10, D32, Dmax (mu) = 63.3888, 86.7386, 179.655 + Liquid penetration 95% mass (m) = 0.0117676 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.202215, Final residual = 7.21285e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.12762, Final residual = 3.4248e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00101949, Final residual = 7.87659e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000610287, Final residual = 4.77375e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000639127, Final residual = 5.47071e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000639124, Final residual = 5.48713e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000981707, Final residual = 7.28105e-08, No Iterations 1 +min/max(T) = 806.026, 2745.34 +GAMG: Solving for p, Initial residual = 0.027023, Final residual = 0.00146046, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.24101e-05, global = 1.41922e-05, cumulative = 0.00682216 +GAMG: Solving for p, Initial residual = 0.00139377, Final residual = 2.09541e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.60385e-05, global = 1.60375e-05, cumulative = 0.0068382 +smoothSolver: Solving for epsilon, Initial residual = 0.000949734, Final residual = 1.26193e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00102025, Final residual = 1.70579e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.10701 s +other Time = 1e-06 s +rho Equations = 0.000177 s +U Equations = 0.001063 s +Y Equations = 0.00239973 s +E Equations = 0.000594 s +p Equations = 0.002426 s +calculate parcels = 139.933 s +chemistry correctThermo = 0.002891 s +turbulence correct = 0.000966 s +combustion correct(in Y) = 0.0963123 s +percentage of chemistry = 90.0031 % +percentage of rho/U/Y/E = 3.95639 % +========Time details of each equation======= +rhoEqn Time = 0.000322 s +rhoEqn assamble = 0.000254 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001062 s +UEqn assamble = 0.000648 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000414 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001829 s +YEqn assamble = 0.000628 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000222 s +YEqn correct boundary = 0 s +EEqn Time = 0.000443 s +EEqn assamble = 0.00033 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 204 s ClockTime = 205 s +Courant Number mean: 0.00136448 max: 0.014491 +Time = 0.0016675 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21970 + Current mass in system = 1.40584e-09 + Linear momentum = (1.60635e-11 -7.63601e-09 0) + |Linear momentum| = 7.63603e-09 + Linear kinetic energy = 2.22191e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 412.712, 540.2 + Mass transfer phase change = 3.00304e-10 + D10, D32, Dmax (mu) = 63.3113, 86.7067, 179.501 + Liquid penetration 95% mass (m) = 0.0117782 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.161158, Final residual = 6.07526e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.125048, Final residual = 3.42165e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00102303, Final residual = 7.99788e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000633736, Final residual = 4.95347e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00066552, Final residual = 5.71942e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000665554, Final residual = 5.73603e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00101112, Final residual = 7.4854e-08, No Iterations 1 +min/max(T) = 806.039, 2747.1 +GAMG: Solving for p, Initial residual = 0.0277273, Final residual = 0.00173975, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.37739e-05, global = 1.3763e-05, cumulative = 0.00685196 +GAMG: Solving for p, Initial residual = 0.00165977, Final residual = 2.49726e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.60208e-05, global = 1.60196e-05, cumulative = 0.00686798 +smoothSolver: Solving for epsilon, Initial residual = 0.000943833, Final residual = 1.26499e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00100695, Final residual = 1.71662e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.110164 s +other Time = 0 s +rho Equations = 0.000185 s +U Equations = 0.001155 s +Y Equations = 0.00245831 s +E Equations = 0.000617 s +p Equations = 0.002405 s +calculate parcels = 140.301 s +chemistry correctThermo = 0.002836 s +turbulence correct = 0.000966 s +combustion correct(in Y) = 0.0993457 s +percentage of chemistry = 90.1798 % +percentage of rho/U/Y/E = 4.00794 % +========Time details of each equation======= +rhoEqn Time = 0.00033 s +rhoEqn assamble = 0.000258 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001153 s +UEqn assamble = 0.000669 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000484 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001826 s +YEqn assamble = 0.00066 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000192 s +YEqn correct boundary = 0 s +EEqn Time = 0.00046 s +EEqn assamble = 0.000344 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 204.48 s ClockTime = 205 s +Courant Number mean: 0.00151708 max: 0.0145474 +Time = 0.00167 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21970 + Current mass in system = 1.40444e-09 + Linear momentum = (1.65353e-11 -7.62331e-09 0) + |Linear momentum| = 7.62333e-09 + Linear kinetic energy = 2.21675e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 412.941, 540.2 + Mass transfer phase change = 3.01698e-10 + D10, D32, Dmax (mu) = 63.2379, 86.6746, 179.288 + Liquid penetration 95% mass (m) = 0.0117894 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.114629, Final residual = 4.39958e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.119257, Final residual = 3.34034e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00102448, Final residual = 8.09896e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000645277, Final residual = 5.06499e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000679794, Final residual = 5.87168e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000679862, Final residual = 5.88854e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00104208, Final residual = 7.6637e-08, No Iterations 1 +min/max(T) = 806.055, 2748.76 +GAMG: Solving for p, Initial residual = 0.0279439, Final residual = 0.0018682, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.47229e-05, global = 1.35897e-05, cumulative = 0.00688157 +GAMG: Solving for p, Initial residual = 0.00178308, Final residual = 2.53879e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.6068e-05, global = 1.60666e-05, cumulative = 0.00689764 +smoothSolver: Solving for epsilon, Initial residual = 0.000934546, Final residual = 1.26162e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000991122, Final residual = 1.71253e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.077634 s +other Time = 0 s +rho Equations = 0.000197 s +U Equations = 0.001116 s +Y Equations = 0.00218999 s +E Equations = 0.000593 s +p Equations = 0.002116 s +calculate parcels = 140.603 s +chemistry correctThermo = 0.001989 s +turbulence correct = 0.000897 s +combustion correct(in Y) = 0.068334 s +percentage of chemistry = 88.0207 % +percentage of rho/U/Y/E = 5.27602 % +========Time details of each equation======= +rhoEqn Time = 0.000326 s +rhoEqn assamble = 0.000257 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001114 s +UEqn assamble = 0.000685 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000429 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001611 s +YEqn assamble = 0.000552 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000132 s +YEqn correct boundary = 0 s +EEqn Time = 0.00047 s +EEqn assamble = 0.000367 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000103 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 204.86 s ClockTime = 205 s +Courant Number mean: 0.00166231 max: 0.0145067 +Time = 0.0016725 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21970 + Current mass in system = 1.40304e-09 + Linear momentum = (1.6959e-11 -7.61048e-09 0) + |Linear momentum| = 7.6105e-09 + Linear kinetic energy = 2.21152e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 413.171, 540.2 + Mass transfer phase change = 3.03099e-10 + D10, D32, Dmax (mu) = 63.1677, 86.6418, 179.072 + Liquid penetration 95% mass (m) = 0.0117992 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0717274, Final residual = 2.60717e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.110776, Final residual = 3.13841e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00102176, Final residual = 8.08901e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000644313, Final residual = 5.10236e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000682039, Final residual = 5.92749e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000682121, Final residual = 5.94438e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00105377, Final residual = 7.68181e-08, No Iterations 1 +min/max(T) = 806.071, 2750.19 +GAMG: Solving for p, Initial residual = 0.02702, Final residual = 0.00181817, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.49506e-05, global = 1.36779e-05, cumulative = 0.00691132 +GAMG: Solving for p, Initial residual = 0.00173655, Final residual = 2.39449e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.61495e-05, global = 1.61481e-05, cumulative = 0.00692747 +smoothSolver: Solving for epsilon, Initial residual = 0.000922319, Final residual = 1.24752e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000970757, Final residual = 1.68956e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.116411 s +other Time = 0 s +rho Equations = 0.00026 s +U Equations = 0.001637 s +Y Equations = 0.00314223 s +E Equations = 0.0007 s +p Equations = 0.003292 s +calculate parcels = 140.942 s +chemistry correctThermo = 0.002922 s +turbulence correct = 0.001305 s +combustion correct(in Y) = 0.102803 s +percentage of chemistry = 88.3102 % +percentage of rho/U/Y/E = 4.93015 % +========Time details of each equation======= +rhoEqn Time = 0.000472 s +rhoEqn assamble = 0.000378 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001636 s +UEqn assamble = 0.001046 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00059 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002331 s +YEqn assamble = 0.000811 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00017 s +YEqn correct boundary = 0 s +EEqn Time = 0.000506 s +EEqn assamble = 0.000383 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000123 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 205.31 s ClockTime = 206 s +Courant Number mean: 0.00178128 max: 0.0150416 +Time = 0.001675 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21970 + Current mass in system = 1.40164e-09 + Linear momentum = (1.73282e-11 -7.59749e-09 0) + |Linear momentum| = 7.59751e-09 + Linear kinetic energy = 2.20621e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 413.402, 540.2 + Mass transfer phase change = 3.04508e-10 + D10, D32, Dmax (mu) = 63.1009, 86.6077, 178.854 + Liquid penetration 95% mass (m) = 0.0118102 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0505201, Final residual = 1.82057e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.10084, Final residual = 2.85241e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00101629, Final residual = 8.01204e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000632444, Final residual = 5.05779e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00067265, Final residual = 5.89206e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000672734, Final residual = 5.90864e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00104385, Final residual = 7.5803e-08, No Iterations 1 +min/max(T) = 806.088, 2751.27 +GAMG: Solving for p, Initial residual = 0.0249463, Final residual = 0.00159494, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.43118e-05, global = 1.39503e-05, cumulative = 0.00694142 +GAMG: Solving for p, Initial residual = 0.00152516, Final residual = 2.01999e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.62376e-05, global = 1.62364e-05, cumulative = 0.00695765 +smoothSolver: Solving for epsilon, Initial residual = 0.000911091, Final residual = 1.22896e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000949757, Final residual = 1.65743e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.116254 s +other Time = 0 s +rho Equations = 0.000303 s +U Equations = 0.001811 s +Y Equations = 0.00402495 s +E Equations = 0.00081 s +p Equations = 0.003408 s +calculate parcels = 141.325 s +chemistry correctThermo = 0.002931 s +turbulence correct = 0.001348 s +combustion correct(in Y) = 0.101315 s +percentage of chemistry = 87.1497 % +percentage of rho/U/Y/E = 5.97739 % +========Time details of each equation======= +rhoEqn Time = 0.000538 s +rhoEqn assamble = 0.000439 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00181 s +UEqn assamble = 0.001203 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000607 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.003193 s +YEqn assamble = 0.001044 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000231 s +YEqn correct boundary = 0 s +EEqn Time = 0.000574 s +EEqn assamble = 0.000446 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000128 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 205.81 s ClockTime = 206 s +Courant Number mean: 0.00187111 max: 0.0154729 +Time = 0.0016775 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21970 + Current mass in system = 1.40022e-09 + Linear momentum = (1.76393e-11 -7.58439e-09 0) + |Linear momentum| = 7.58441e-09 + Linear kinetic energy = 2.20085e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 413.632, 540.2 + Mass transfer phase change = 3.05923e-10 + D10, D32, Dmax (mu) = 63.0371, 86.5726, 178.899 + Liquid penetration 95% mass (m) = 0.0118217 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0737613, Final residual = 3.01118e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0904778, Final residual = 2.53691e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00100544, Final residual = 7.9014e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000613803, Final residual = 4.96264e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000655709, Final residual = 5.7907e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000655801, Final residual = 5.80749e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00101545, Final residual = 7.40481e-08, No Iterations 1 +min/max(T) = 806.107, 2752.02 +GAMG: Solving for p, Initial residual = 0.0221343, Final residual = 0.00126104, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.30295e-05, global = 1.43492e-05, cumulative = 0.006972 +GAMG: Solving for p, Initial residual = 0.00120802, Final residual = 8.30202e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.63148e-05, global = 1.63102e-05, cumulative = 0.00698831 +smoothSolver: Solving for epsilon, Initial residual = 0.000904251, Final residual = 1.21456e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000936146, Final residual = 1.63245e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100974 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001446 s +Y Equations = 0.00248671 s +E Equations = 0.000589 s +p Equations = 0.0023 s +calculate parcels = 141.701 s +chemistry correctThermo = 0.00289 s +turbulence correct = 0.000995 s +combustion correct(in Y) = 0.0898853 s +percentage of chemistry = 89.0183 % +percentage of rho/U/Y/E = 4.65339 % +========Time details of each equation======= +rhoEqn Time = 0.000324 s +rhoEqn assamble = 0.000256 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001444 s +UEqn assamble = 0.000886 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000558 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001792 s +YEqn assamble = 0.00067 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000161 s +YEqn correct boundary = 0 s +EEqn Time = 0.000434 s +EEqn assamble = 0.000324 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00011 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 206.29 s ClockTime = 207 s +Courant Number mean: 0.00194206 max: 0.0159194 +Time = 0.00168 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21970 + Current mass in system = 1.3988e-09 + Linear momentum = (1.78875e-11 -7.57123e-09 0) + |Linear momentum| = 7.57125e-09 + Linear kinetic energy = 2.19546e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 413.861, 540.2 + Mass transfer phase change = 3.07342e-10 + D10, D32, Dmax (mu) = 62.9737, 86.5369, 179.413 + Liquid penetration 95% mass (m) = 0.0118332 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.102174, Final residual = 4.2629e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0819157, Final residual = 2.28718e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000992213, Final residual = 7.76914e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000591484, Final residual = 4.83028e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000634856, Final residual = 5.65242e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00063493, Final residual = 5.66867e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000975725, Final residual = 7.18858e-08, No Iterations 1 +min/max(T) = 806.126, 2752.46 +GAMG: Solving for p, Initial residual = 0.0202779, Final residual = 0.000923355, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.15755e-05, global = 1.47671e-05, cumulative = 0.00700308 +GAMG: Solving for p, Initial residual = 0.000886005, Final residual = 5.12475e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.63596e-05, global = 1.63569e-05, cumulative = 0.00701944 +smoothSolver: Solving for epsilon, Initial residual = 0.000900301, Final residual = 1.20312e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000936591, Final residual = 1.62308e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.091893 s +other Time = 0 s +rho Equations = 0.000152 s +U Equations = 0.00111 s +Y Equations = 0.00239769 s +E Equations = 0.000599 s +p Equations = 0.002193 s +calculate parcels = 142.036 s +chemistry correctThermo = 0.002892 s +turbulence correct = 0.000995 s +combustion correct(in Y) = 0.0813713 s +percentage of chemistry = 88.5501 % +percentage of rho/U/Y/E = 4.6344 % +========Time details of each equation======= +rhoEqn Time = 0.000304 s +rhoEqn assamble = 0.000229 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001109 s +UEqn assamble = 0.000683 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000426 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001815 s +YEqn assamble = 0.000622 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000213 s +YEqn correct boundary = 0 s +EEqn Time = 0.000442 s +EEqn assamble = 0.00033 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 206.71 s ClockTime = 207 s +Courant Number mean: 0.00201138 max: 0.0163253 +Time = 0.0016825 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21970 + Current mass in system = 1.39738e-09 + Linear momentum = (1.80796e-11 -7.55814e-09 0) + |Linear momentum| = 7.55816e-09 + Linear kinetic energy = 2.19011e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 414.087, 540.2 + Mass transfer phase change = 3.08762e-10 + D10, D32, Dmax (mu) = 62.9101, 86.5012, 179.904 + Liquid penetration 95% mass (m) = 0.0118442 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.124138, Final residual = 5.03952e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0762552, Final residual = 2.12644e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000978952, Final residual = 7.67221e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00057113, Final residual = 4.73896e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000616153, Final residual = 5.53365e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00061618, Final residual = 5.54931e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000944093, Final residual = 7.00148e-08, No Iterations 1 +min/max(T) = 806.146, 2752.69 +GAMG: Solving for p, Initial residual = 0.0203762, Final residual = 0.000857224, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.13387e-05, global = 1.51517e-05, cumulative = 0.00703459 +GAMG: Solving for p, Initial residual = 0.000826758, Final residual = 4.80289e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.63649e-05, global = 1.63628e-05, cumulative = 0.00705095 +smoothSolver: Solving for epsilon, Initial residual = 0.000898064, Final residual = 1.19383e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00094466, Final residual = 1.62413e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.105784 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.00121 s +Y Equations = 0.00242198 s +E Equations = 0.000619 s +p Equations = 0.002234 s +calculate parcels = 142.403 s +chemistry correctThermo = 0.002859 s +turbulence correct = 0.001033 s +combustion correct(in Y) = 0.09503 s +percentage of chemistry = 89.834 % +percentage of rho/U/Y/E = 4.18587 % +========Time details of each equation======= +rhoEqn Time = 0.000321 s +rhoEqn assamble = 0.000257 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001208 s +UEqn assamble = 0.000728 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00048 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001789 s +YEqn assamble = 0.000631 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000209 s +YEqn correct boundary = 0 s +EEqn Time = 0.000446 s +EEqn assamble = 0.000329 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 207.19 s ClockTime = 208 s +Courant Number mean: 0.00209134 max: 0.0167326 +Time = 0.001685 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21969 + Current mass in system = 1.39596e-09 + Linear momentum = (1.82258e-11 -7.54519e-09 0) + |Linear momentum| = 7.54521e-09 + Linear kinetic energy = 2.18484e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 414.311, 540.2 + Mass transfer phase change = 3.10186e-10 + D10, D32, Dmax (mu) = 62.9128, 86.4694, 179.698 + Liquid penetration 95% mass (m) = 0.0118564 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.13165, Final residual = 5.13968e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.070873, Final residual = 1.99173e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000976369, Final residual = 7.64164e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000556334, Final residual = 4.67955e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000603042, Final residual = 5.43847e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000603022, Final residual = 5.45369e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000931985, Final residual = 6.87621e-08, No Iterations 1 +min/max(T) = 806.166, 2752.8 +GAMG: Solving for p, Initial residual = 0.0217484, Final residual = 0.000993473, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.22451e-05, global = 1.55209e-05, cumulative = 0.00706647 +GAMG: Solving for p, Initial residual = 0.000959795, Final residual = 6.6216e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.64251e-05, global = 1.64223e-05, cumulative = 0.00708289 +smoothSolver: Solving for epsilon, Initial residual = 0.000899151, Final residual = 1.18873e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000956052, Final residual = 1.63349e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.109062 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001351 s +Y Equations = 0.00270011 s +E Equations = 0.000624 s +p Equations = 0.001948 s +calculate parcels = 142.766 s +chemistry correctThermo = 0.002103 s +turbulence correct = 0.000954 s +combustion correct(in Y) = 0.0989989 s +percentage of chemistry = 90.773 % +percentage of rho/U/Y/E = 4.44894 % +========Time details of each equation======= +rhoEqn Time = 0.000307 s +rhoEqn assamble = 0.000242 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001351 s +UEqn assamble = 0.000815 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000536 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002038 s +YEqn assamble = 0.000722 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000197 s +YEqn correct boundary = 0 s +EEqn Time = 0.000459 s +EEqn assamble = 0.000342 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 207.66 s ClockTime = 208 s +Courant Number mean: 0.00217557 max: 0.0171933 +Time = 0.0016875 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21969 + Current mass in system = 1.39455e-09 + Linear momentum = (1.83442e-11 -7.53256e-09 0) + |Linear momentum| = 7.53259e-09 + Linear kinetic energy = 2.17973e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 414.53, 540.2 + Mass transfer phase change = 3.11594e-10 + D10, D32, Dmax (mu) = 62.8457, 86.4344, 179.478 + Liquid penetration 95% mass (m) = 0.011867 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.117779, Final residual = 4.42005e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.065476, Final residual = 1.87128e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000958206, Final residual = 7.51612e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000550152, Final residual = 4.65869e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000601351, Final residual = 5.44773e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000601279, Final residual = 5.46328e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000935335, Final residual = 6.81572e-08, No Iterations 1 +min/max(T) = 806.187, 2752.87 +GAMG: Solving for p, Initial residual = 0.0230426, Final residual = 0.00109866, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.27143e-05, global = 1.55322e-05, cumulative = 0.00709843 +GAMG: Solving for p, Initial residual = 0.001062, Final residual = 7.18176e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.62336e-05, global = 1.62305e-05, cumulative = 0.00711466 +smoothSolver: Solving for epsilon, Initial residual = 0.000903239, Final residual = 1.18751e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000966354, Final residual = 1.6471e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.078687 s +other Time = 0 s +rho Equations = 0.000166 s +U Equations = 0.001076 s +Y Equations = 0.0023219 s +E Equations = 0.000477 s +p Equations = 0.002401 s +calculate parcels = 143.037 s +chemistry correctThermo = 0.001984 s +turbulence correct = 0.001015 s +combustion correct(in Y) = 0.0690161 s +percentage of chemistry = 87.7097 % +percentage of rho/U/Y/E = 5.1354 % +========Time details of each equation======= +rhoEqn Time = 0.000314 s +rhoEqn assamble = 0.000248 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001076 s +UEqn assamble = 0.000646 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00043 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001714 s +YEqn assamble = 0.000528 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000111 s +YEqn correct boundary = 0 s +EEqn Time = 0.000358 s +EEqn assamble = 0.000267 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 208.01 s ClockTime = 209 s +Courant Number mean: 0.00227649 max: 0.017714 +Time = 0.00169 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21967 + Current mass in system = 1.39314e-09 + Linear momentum = (1.84477e-11 -7.52024e-09 0) + |Linear momentum| = 7.52027e-09 + Linear kinetic energy = 2.17477e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 414.744, 540.2 + Mass transfer phase change = 3.12999e-10 + D10, D32, Dmax (mu) = 62.983, 86.4059, 179.263 + Liquid penetration 95% mass (m) = 0.0118786 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0836654, Final residual = 3.08446e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0599495, Final residual = 1.76065e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000953538, Final residual = 7.54598e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000549883, Final residual = 4.6962e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000603023, Final residual = 5.49644e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000602922, Final residual = 5.51221e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000941336, Final residual = 6.83462e-08, No Iterations 1 +min/max(T) = 806.208, 2752.98 +GAMG: Solving for p, Initial residual = 0.0237029, Final residual = 0.00111724, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.2807e-05, global = 1.56118e-05, cumulative = 0.00713027 +GAMG: Solving for p, Initial residual = 0.00108023, Final residual = 8.40129e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.61917e-05, global = 1.61881e-05, cumulative = 0.00714646 +smoothSolver: Solving for epsilon, Initial residual = 0.000910194, Final residual = 1.18885e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000973097, Final residual = 1.66359e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.107434 s +other Time = 0 s +rho Equations = 0.000183 s +U Equations = 0.001282 s +Y Equations = 0.00242987 s +E Equations = 0.000602 s +p Equations = 0.002266 s +calculate parcels = 143.389 s +chemistry correctThermo = 0.002881 s +turbulence correct = 0.001104 s +combustion correct(in Y) = 0.0964781 s +percentage of chemistry = 89.8022 % +percentage of rho/U/Y/E = 4.18571 % +========Time details of each equation======= +rhoEqn Time = 0.000331 s +rhoEqn assamble = 0.00026 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001281 s +UEqn assamble = 0.000783 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000498 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001803 s +YEqn assamble = 0.000632 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00018 s +YEqn correct boundary = 0 s +EEqn Time = 0.000446 s +EEqn assamble = 0.000334 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 208.47 s ClockTime = 209 s +Courant Number mean: 0.00239763 max: 0.0183062 +Time = 0.0016925 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21967 + Current mass in system = 1.39176e-09 + Linear momentum = (1.85554e-11 -7.50831e-09 0) + |Linear momentum| = 7.50833e-09 + Linear kinetic energy = 2.16999e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 414.954, 540.2 + Mass transfer phase change = 3.14383e-10 + D10, D32, Dmax (mu) = 62.9112, 86.3742, 179.67 + Liquid penetration 95% mass (m) = 0.011892 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.054652, Final residual = 2.23937e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0547069, Final residual = 1.66495e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00094093, Final residual = 7.53047e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000553956, Final residual = 4.78504e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000610846, Final residual = 5.63378e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000610782, Final residual = 5.64971e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000944958, Final residual = 6.88498e-08, No Iterations 1 +min/max(T) = 806.229, 2753.05 +GAMG: Solving for p, Initial residual = 0.0235163, Final residual = 0.00104422, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.2152e-05, global = 1.5391e-05, cumulative = 0.00716185 +GAMG: Solving for p, Initial residual = 0.00101008, Final residual = 7.92394e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.59608e-05, global = 1.59575e-05, cumulative = 0.00717781 +smoothSolver: Solving for epsilon, Initial residual = 0.000917392, Final residual = 1.19514e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000978497, Final residual = 1.6894e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.090042 s +other Time = 0 s +rho Equations = 0.000152 s +U Equations = 0.001108 s +Y Equations = 0.00215033 s +E Equations = 0.0005 s +p Equations = 0.001852 s +calculate parcels = 143.745 s +chemistry correctThermo = 0.002058 s +turbulence correct = 0.000923 s +combustion correct(in Y) = 0.0811217 s +percentage of chemistry = 90.0931 % +percentage of rho/U/Y/E = 4.34278 % +========Time details of each equation======= +rhoEqn Time = 0.00027 s +rhoEqn assamble = 0.000212 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001107 s +UEqn assamble = 0.000663 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000444 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001567 s +YEqn assamble = 0.000556 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000145 s +YEqn correct boundary = 0 s +EEqn Time = 0.000376 s +EEqn assamble = 0.000281 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 208.92 s ClockTime = 209 s +Courant Number mean: 0.00252342 max: 0.0189459 +Time = 0.001695 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21966 + Current mass in system = 1.39038e-09 + Linear momentum = (1.86704e-11 -7.49664e-09 0) + |Linear momentum| = 7.49666e-09 + Linear kinetic energy = 2.16536e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 415.161, 540.2 + Mass transfer phase change = 3.15767e-10 + D10, D32, Dmax (mu) = 62.8977, 86.3474, 180.13 + Liquid penetration 95% mass (m) = 0.011903 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0688834, Final residual = 2.98527e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0499697, Final residual = 1.57767e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000946435, Final residual = 7.69261e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000561982, Final residual = 4.92379e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0006213, Final residual = 5.79532e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000621235, Final residual = 5.81125e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000946665, Final residual = 6.9927e-08, No Iterations 1 +min/max(T) = 806.25, 2753.14 +GAMG: Solving for p, Initial residual = 0.0227222, Final residual = 0.000888669, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.12078e-05, global = 1.53357e-05, cumulative = 0.00719314 +GAMG: Solving for p, Initial residual = 0.000859309, Final residual = 7.16594e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.59504e-05, global = 1.59475e-05, cumulative = 0.00720909 +smoothSolver: Solving for epsilon, Initial residual = 0.000925387, Final residual = 1.20797e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000984649, Final residual = 1.72072e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097411 s +other Time = 0 s +rho Equations = 0.000195 s +U Equations = 0.001194 s +Y Equations = 0.00212963 s +E Equations = 0.000485 s +p Equations = 0.001795 s +calculate parcels = 144.096 s +chemistry correctThermo = 0.002003 s +turbulence correct = 0.000806 s +combustion correct(in Y) = 0.0886044 s +percentage of chemistry = 90.9593 % +percentage of rho/U/Y/E = 4.11004 % +========Time details of each equation======= +rhoEqn Time = 0.000313 s +rhoEqn assamble = 0.000244 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001192 s +UEqn assamble = 0.00068 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000512 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001432 s +YEqn assamble = 0.000525 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 6.6e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000364 s +EEqn assamble = 0.000272 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 209.36 s ClockTime = 210 s +Courant Number mean: 0.00265215 max: 0.0196551 +Time = 0.0016975 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21964 + Current mass in system = 1.38899e-09 + Linear momentum = (1.8813e-11 -7.48517e-09 0) + |Linear momentum| = 7.48519e-09 + Linear kinetic energy = 2.16083e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 415.364, 540.2 + Mass transfer phase change = 3.17148e-10 + D10, D32, Dmax (mu) = 62.9622, 86.3238, 179.937 + Liquid penetration 95% mass (m) = 0.0119138 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0828797, Final residual = 3.7164e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0457421, Final residual = 1.49405e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000949222, Final residual = 7.80222e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000573015, Final residual = 5.08791e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000634947, Final residual = 6.00013e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000634916, Final residual = 6.01644e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000947281, Final residual = 7.10166e-08, No Iterations 1 +min/max(T) = 806.266, 2753.26 +GAMG: Solving for p, Initial residual = 0.0216595, Final residual = 0.000683846, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.99327e-05, global = 1.51891e-05, cumulative = 0.00722428 +GAMG: Solving for p, Initial residual = 0.000661401, Final residual = 4.47766e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.59237e-05, global = 1.59219e-05, cumulative = 0.0072402 +smoothSolver: Solving for epsilon, Initial residual = 0.000930873, Final residual = 1.22288e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000988638, Final residual = 1.75306e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102984 s +other Time = 0 s +rho Equations = 0.000181 s +U Equations = 0.001205 s +Y Equations = 0.00243217 s +E Equations = 0.000591 s +p Equations = 0.002132 s +calculate parcels = 144.438 s +chemistry correctThermo = 0.00209 s +turbulence correct = 0.000981 s +combustion correct(in Y) = 0.0931688 s +percentage of chemistry = 90.4692 % +percentage of rho/U/Y/E = 4.28141 % +========Time details of each equation======= +rhoEqn Time = 0.00031 s +rhoEqn assamble = 0.000242 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001204 s +UEqn assamble = 0.000695 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000509 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001793 s +YEqn assamble = 0.000638 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000182 s +YEqn correct boundary = 0 s +EEqn Time = 0.000438 s +EEqn assamble = 0.000324 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 209.81 s ClockTime = 210 s +Courant Number mean: 0.00278432 max: 0.0203023 +Time = 0.0017 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21963 + Current mass in system = 1.38762e-09 + Linear momentum = (1.8977e-11 -7.47381e-09 0) + |Linear momentum| = 7.47384e-09 + Linear kinetic energy = 2.15636e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 415.564, 540.2 + Mass transfer phase change = 3.18523e-10 + D10, D32, Dmax (mu) = 62.9449, 86.298, 179.746 + Liquid penetration 95% mass (m) = 0.0119259 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0881041, Final residual = 4.117e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0420043, Final residual = 1.41215e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000945497, Final residual = 7.81135e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000583589, Final residual = 5.22288e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000648719, Final residual = 6.19662e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000648715, Final residual = 6.21446e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000943592, Final residual = 7.15042e-08, No Iterations 1 +min/max(T) = 806.254, 2753.43 +GAMG: Solving for p, Initial residual = 0.0209118, Final residual = 0.000586286, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.90891e-05, global = 1.49546e-05, cumulative = 0.00725515 +GAMG: Solving for p, Initial residual = 0.000566385, Final residual = 4.06408e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.58486e-05, global = 1.58468e-05, cumulative = 0.007271 +smoothSolver: Solving for epsilon, Initial residual = 0.000931269, Final residual = 1.23245e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000988652, Final residual = 1.78182e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.076298 s +other Time = 0 s +rho Equations = 0.00017 s +U Equations = 0.001047 s +Y Equations = 0.00213712 s +E Equations = 0.000481 s +p Equations = 0.001842 s +calculate parcels = 144.764 s +chemistry correctThermo = 0.001993 s +turbulence correct = 0.000899 s +combustion correct(in Y) = 0.0675509 s +percentage of chemistry = 88.5356 % +percentage of rho/U/Y/E = 5.0265 % +========Time details of each equation======= +rhoEqn Time = 0.000291 s +rhoEqn assamble = 0.000232 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001047 s +UEqn assamble = 0.000618 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000429 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00154 s +YEqn assamble = 0.000528 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000114 s +YEqn correct boundary = 0 s +EEqn Time = 0.000358 s +EEqn assamble = 0.000267 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 210.5 s ClockTime = 211 s +Courant Number mean: 0.00291934 max: 0.0209317 +Time = 0.0017025 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21962 + Current mass in system = 1.38624e-09 + Linear momentum = (1.91709e-11 -7.46244e-09 0) + |Linear momentum| = 7.46247e-09 + Linear kinetic energy = 2.1519e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 415.763, 540.2 + Mass transfer phase change = 3.19899e-10 + D10, D32, Dmax (mu) = 62.9316, 86.2718, 179.556 + Liquid penetration 95% mass (m) = 0.0119371 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0835943, Final residual = 4.0636e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0390792, Final residual = 1.33281e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000944477, Final residual = 7.85708e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000592334, Final residual = 5.37489e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000659736, Final residual = 6.40286e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000659743, Final residual = 6.42114e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000939345, Final residual = 7.22551e-08, No Iterations 1 +min/max(T) = 806.245, 2753.61 +GAMG: Solving for p, Initial residual = 0.0208946, Final residual = 0.000638873, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.92776e-05, global = 1.48262e-05, cumulative = 0.00728583 +GAMG: Solving for p, Initial residual = 0.000617393, Final residual = 4.72686e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.58605e-05, global = 1.5858e-05, cumulative = 0.00730168 +smoothSolver: Solving for epsilon, Initial residual = 0.000928827, Final residual = 1.23609e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000985972, Final residual = 1.80462e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.084694 s +other Time = 0 s +rho Equations = 0.000154 s +U Equations = 0.001011 s +Y Equations = 0.00212126 s +E Equations = 0.000475 s +p Equations = 0.001834 s +calculate parcels = 145.081 s +chemistry correctThermo = 0.002016 s +turbulence correct = 0.000841 s +combustion correct(in Y) = 0.0760587 s +percentage of chemistry = 89.8042 % +percentage of rho/U/Y/E = 4.44099 % +========Time details of each equation======= +rhoEqn Time = 0.000272 s +rhoEqn assamble = 0.000215 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00101 s +UEqn assamble = 0.000589 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000421 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001576 s +YEqn assamble = 0.000585 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000152 s +YEqn correct boundary = 0 s +EEqn Time = 0.000358 s +EEqn assamble = 0.000267 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 210.9 s ClockTime = 211 s +Courant Number mean: 0.00305325 max: 0.0214747 +Time = 0.001705 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21962 + Current mass in system = 1.38487e-09 + Linear momentum = (1.9389e-11 -7.45103e-09 0) + |Linear momentum| = 7.45105e-09 + Linear kinetic energy = 2.1474e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 415.961, 540.2 + Mass transfer phase change = 3.2127e-10 + D10, D32, Dmax (mu) = 62.8643, 86.2413, 179.366 + Liquid penetration 95% mass (m) = 0.0119487 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.070428, Final residual = 3.52395e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0369308, Final residual = 1.26318e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000938309, Final residual = 7.81008e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000597244, Final residual = 5.4579e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000667275, Final residual = 6.54266e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000667288, Final residual = 6.56133e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000938127, Final residual = 7.25416e-08, No Iterations 1 +min/max(T) = 806.237, 2753.79 +GAMG: Solving for p, Initial residual = 0.0211766, Final residual = 0.000724499, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.96449e-05, global = 1.46794e-05, cumulative = 0.00731636 +GAMG: Solving for p, Initial residual = 0.000701759, Final residual = 5.43378e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.58054e-05, global = 1.58025e-05, cumulative = 0.00733217 +smoothSolver: Solving for epsilon, Initial residual = 0.00092254, Final residual = 1.23228e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00098075, Final residual = 1.8193e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.10658 s +other Time = 0 s +rho Equations = 0.000257 s +U Equations = 0.001806 s +Y Equations = 0.00259642 s +E Equations = 0.000604 s +p Equations = 0.002296 s +calculate parcels = 145.434 s +chemistry correctThermo = 0.00291 s +turbulence correct = 0.001049 s +combustion correct(in Y) = 0.0947906 s +percentage of chemistry = 88.9384 % +percentage of rho/U/Y/E = 4.93847 % +========Time details of each equation======= +rhoEqn Time = 0.000404 s +rhoEqn assamble = 0.000311 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001804 s +UEqn assamble = 0.000963 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000841 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001477 s +YEqn assamble = 0.000614 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -7.5e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000452 s +EEqn assamble = 0.000326 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000126 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 211.36 s ClockTime = 212 s +Courant Number mean: 0.00318152 max: 0.0220095 +Time = 0.0017075 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21962 + Current mass in system = 1.38349e-09 + Linear momentum = (1.96257e-11 -7.43948e-09 0) + |Linear momentum| = 7.4395e-09 + Linear kinetic energy = 2.14284e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 416.158, 540.2 + Mass transfer phase change = 3.22648e-10 + D10, D32, Dmax (mu) = 62.7984, 86.2095, 179.175 + Liquid penetration 95% mass (m) = 0.0119607 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0526942, Final residual = 2.66305e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0351804, Final residual = 1.20222e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000938376, Final residual = 7.82186e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000598497, Final residual = 5.53154e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00066978, Final residual = 6.64468e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000669805, Final residual = 6.66353e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000938509, Final residual = 7.28719e-08, No Iterations 1 +min/max(T) = 806.232, 2753.92 +GAMG: Solving for p, Initial residual = 0.0214525, Final residual = 0.00077106, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.99028e-05, global = 1.47418e-05, cumulative = 0.00734691 +GAMG: Solving for p, Initial residual = 0.000748334, Final residual = 4.95293e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.58811e-05, global = 1.58784e-05, cumulative = 0.00736279 +smoothSolver: Solving for epsilon, Initial residual = 0.000915179, Final residual = 1.22079e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00097486, Final residual = 1.82453e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.091027 s +other Time = 0 s +rho Equations = 0.000153 s +U Equations = 0.00098 s +Y Equations = 0.00248593 s +E Equations = 0.000608 s +p Equations = 0.002532 s +calculate parcels = 145.773 s +chemistry correctThermo = 0.002865 s +turbulence correct = 0.001129 s +combustion correct(in Y) = 0.0800961 s +percentage of chemistry = 87.9916 % +percentage of rho/U/Y/E = 4.6436 % +========Time details of each equation======= +rhoEqn Time = 0.000315 s +rhoEqn assamble = 0.000248 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000979 s +UEqn assamble = 0.000572 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000407 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001941 s +YEqn assamble = 0.000651 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000271 s +YEqn correct boundary = 0 s +EEqn Time = 0.000449 s +EEqn assamble = 0.000334 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 211.79 s ClockTime = 212 s +Courant Number mean: 0.00329965 max: 0.0224348 +Time = 0.00171 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21961 + Current mass in system = 1.3821e-09 + Linear momentum = (1.98677e-11 -7.42772e-09 0) + |Linear momentum| = 7.42774e-09 + Linear kinetic energy = 2.1382e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 416.354, 540.2 + Mass transfer phase change = 3.24044e-10 + D10, D32, Dmax (mu) = 62.7943, 86.1804, 178.983 + Liquid penetration 95% mass (m) = 0.0119718 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0342476, Final residual = 1.71923e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0335639, Final residual = 1.1406e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000945506, Final residual = 7.85253e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00059611, Final residual = 5.54762e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000667097, Final residual = 6.66302e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000667128, Final residual = 6.68193e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000936553, Final residual = 7.26011e-08, No Iterations 1 +min/max(T) = 806.229, 2753.98 +GAMG: Solving for p, Initial residual = 0.0217506, Final residual = 0.000763426, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.99968e-05, global = 1.5024e-05, cumulative = 0.00737781 +GAMG: Solving for p, Initial residual = 0.000742052, Final residual = 4.29576e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.60977e-05, global = 1.60955e-05, cumulative = 0.00739391 +smoothSolver: Solving for epsilon, Initial residual = 0.000908867, Final residual = 1.20678e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000969967, Final residual = 1.82517e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.10481 s +other Time = 0 s +rho Equations = 0.000196 s +U Equations = 0.001235 s +Y Equations = 0.00243637 s +E Equations = 0.000626 s +p Equations = 0.002277 s +calculate parcels = 146.111 s +chemistry correctThermo = 0.002957 s +turbulence correct = 0.001042 s +combustion correct(in Y) = 0.0938346 s +percentage of chemistry = 89.5283 % +percentage of rho/U/Y/E = 4.28716 % +========Time details of each equation======= +rhoEqn Time = 0.000339 s +rhoEqn assamble = 0.000259 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001234 s +UEqn assamble = 0.000748 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000486 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001878 s +YEqn assamble = 0.000642 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000257 s +YEqn correct boundary = 0 s +EEqn Time = 0.000471 s +EEqn assamble = 0.000353 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 212.23 s ClockTime = 213 s +Courant Number mean: 0.0034044 max: 0.0227665 +Time = 0.0017125 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21960 + Current mass in system = 1.38069e-09 + Linear momentum = (2.01171e-11 -7.41578e-09 0) + |Linear momentum| = 7.41581e-09 + Linear kinetic energy = 2.13348e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 416.551, 540.2 + Mass transfer phase change = 3.25449e-10 + D10, D32, Dmax (mu) = 62.7941, 86.1501, 178.789 + Liquid penetration 95% mass (m) = 0.0119843 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0306912, Final residual = 1.42084e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0319685, Final residual = 1.0784e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000940373, Final residual = 7.77317e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000589763, Final residual = 5.53802e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000661451, Final residual = 6.63478e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000661472, Final residual = 6.65361e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000929867, Final residual = 7.19247e-08, No Iterations 1 +min/max(T) = 806.23, 2753.94 +GAMG: Solving for p, Initial residual = 0.0220294, Final residual = 0.000702478, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.9798e-05, global = 1.52445e-05, cumulative = 0.00740915 +GAMG: Solving for p, Initial residual = 0.000683541, Final residual = 5.0572e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.61885e-05, global = 1.61859e-05, cumulative = 0.00742534 +smoothSolver: Solving for epsilon, Initial residual = 0.000901971, Final residual = 1.19041e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000965752, Final residual = 1.82049e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.075819 s +other Time = 1e-06 s +rho Equations = 0.000171 s +U Equations = 0.001243 s +Y Equations = 0.00217017 s +E Equations = 0.000511 s +p Equations = 0.001787 s +calculate parcels = 146.446 s +chemistry correctThermo = 0.00196 s +turbulence correct = 0.000826 s +combustion correct(in Y) = 0.0669258 s +percentage of chemistry = 88.2705 % +percentage of rho/U/Y/E = 5.40125 % +========Time details of each equation======= +rhoEqn Time = 0.000287 s +rhoEqn assamble = 0.000229 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001241 s +UEqn assamble = 0.000801 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00044 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001597 s +YEqn assamble = 0.000556 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000129 s +YEqn correct boundary = 0 s +EEqn Time = 0.000386 s +EEqn assamble = 0.000279 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000107 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 212.64 s ClockTime = 213 s +Courant Number mean: 0.00349482 max: 0.0230367 +Time = 0.001715 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21960 + Current mass in system = 1.37929e-09 + Linear momentum = (2.03646e-11 -7.40374e-09 0) + |Linear momentum| = 7.40377e-09 + Linear kinetic energy = 2.12869e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 416.749, 540.2 + Mass transfer phase change = 3.26848e-10 + D10, D32, Dmax (mu) = 62.7338, 86.1144, 178.595 + Liquid penetration 95% mass (m) = 0.0119967 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0381918, Final residual = 1.84523e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0303233, Final residual = 1.01886e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000924716, Final residual = 7.56438e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000580059, Final residual = 5.47286e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000653315, Final residual = 6.57715e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000653327, Final residual = 6.59638e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000917925, Final residual = 7.04443e-08, No Iterations 1 +min/max(T) = 806.235, 2753.8 +GAMG: Solving for p, Initial residual = 0.0222974, Final residual = 0.000589842, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.92874e-05, global = 1.53769e-05, cumulative = 0.00744071 +GAMG: Solving for p, Initial residual = 0.000573982, Final residual = 5.11881e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.6132e-05, global = 1.61294e-05, cumulative = 0.00745684 +smoothSolver: Solving for epsilon, Initial residual = 0.000893642, Final residual = 1.17356e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000961447, Final residual = 1.81296e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.112998 s +other Time = 0 s +rho Equations = 0.000171 s +U Equations = 0.001237 s +Y Equations = 0.00210721 s +E Equations = 0.000513 s +p Equations = 0.003446 s +calculate parcels = 146.725 s +chemistry correctThermo = 0.002038 s +turbulence correct = 0.001649 s +combustion correct(in Y) = 0.101635 s +percentage of chemistry = 89.9439 % +percentage of rho/U/Y/E = 3.56485 % +========Time details of each equation======= +rhoEqn Time = 0.000448 s +rhoEqn assamble = 0.000335 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000113 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001237 s +UEqn assamble = 0.000756 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000481 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001454 s +YEqn assamble = 0.000526 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.4e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.00039 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 213.04 s ClockTime = 214 s +Courant Number mean: 0.00357281 max: 0.0232663 +Time = 0.0017175 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21960 + Current mass in system = 1.37789e-09 + Linear momentum = (2.05929e-11 -7.3916e-09 0) + |Linear momentum| = 7.39163e-09 + Linear kinetic energy = 2.12386e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 416.948, 540.2 + Mass transfer phase change = 3.28252e-10 + D10, D32, Dmax (mu) = 62.6737, 86.0779, 178.401 + Liquid penetration 95% mass (m) = 0.0120074 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0467302, Final residual = 2.31225e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.028719, Final residual = 9.62413e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000915622, Final residual = 7.47687e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000570179, Final residual = 5.41892e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000643384, Final residual = 6.49677e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000643392, Final residual = 6.51563e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000907302, Final residual = 6.9256e-08, No Iterations 1 +min/max(T) = 806.243, 2753.56 +GAMG: Solving for p, Initial residual = 0.0226554, Final residual = 0.000472223, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.87247e-05, global = 1.56214e-05, cumulative = 0.00747246 +GAMG: Solving for p, Initial residual = 0.00045928, Final residual = 2.56544e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.61821e-05, global = 1.61809e-05, cumulative = 0.00748865 +smoothSolver: Solving for epsilon, Initial residual = 0.000888381, Final residual = 1.15953e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000958554, Final residual = 1.80466e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.117681 s +other Time = 1e-06 s +rho Equations = 0.000223 s +U Equations = 0.001422 s +Y Equations = 0.00245201 s +E Equations = 0.000597 s +p Equations = 0.002213 s +calculate parcels = 147.098 s +chemistry correctThermo = 0.002908 s +turbulence correct = 0.000981 s +combustion correct(in Y) = 0.106671 s +percentage of chemistry = 90.6442 % +percentage of rho/U/Y/E = 3.98876 % +========Time details of each equation======= +rhoEqn Time = 0.000365 s +rhoEqn assamble = 0.000288 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00142 s +UEqn assamble = 0.000868 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000552 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001763 s +YEqn assamble = 0.000626 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000165 s +YEqn correct boundary = 0 s +EEqn Time = 0.000443 s +EEqn assamble = 0.00033 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 213.53 s ClockTime = 214 s +Courant Number mean: 0.00364098 max: 0.0234454 +Time = 0.00172 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21960 + Current mass in system = 1.37648e-09 + Linear momentum = (2.07935e-11 -7.37943e-09 0) + |Linear momentum| = 7.37946e-09 + Linear kinetic energy = 2.11901e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 417.147, 540.2 + Mass transfer phase change = 3.29658e-10 + D10, D32, Dmax (mu) = 62.6136, 86.0408, 178.208 + Liquid penetration 95% mass (m) = 0.0120187 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0527112, Final residual = 2.6183e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0273198, Final residual = 9.14312e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000907643, Final residual = 7.43744e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000561795, Final residual = 5.3628e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000634859, Final residual = 6.42231e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000634857, Final residual = 6.44108e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000900135, Final residual = 6.82786e-08, No Iterations 1 +min/max(T) = 806.254, 2753.27 +GAMG: Solving for p, Initial residual = 0.0233626, Final residual = 0.00045858, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.86442e-05, global = 1.58068e-05, cumulative = 0.00750445 +GAMG: Solving for p, Initial residual = 0.000446427, Final residual = 3.19585e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.62107e-05, global = 1.62095e-05, cumulative = 0.00752066 +smoothSolver: Solving for epsilon, Initial residual = 0.000886973, Final residual = 1.15031e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000958214, Final residual = 1.79946e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.101116 s +other Time = 0 s +rho Equations = 0.000184 s +U Equations = 0.001251 s +Y Equations = 0.00208758 s +E Equations = 0.00049 s +p Equations = 0.003659 s +calculate parcels = 147.461 s +chemistry correctThermo = 0.002009 s +turbulence correct = 0.001415 s +combustion correct(in Y) = 0.0898074 s +percentage of chemistry = 88.8162 % +percentage of rho/U/Y/E = 3.9683 % +========Time details of each equation======= +rhoEqn Time = 0.000502 s +rhoEqn assamble = 0.000378 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000124 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00125 s +UEqn assamble = 0.000755 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000495 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001458 s +YEqn assamble = 0.000522 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000114 s +YEqn correct boundary = 0 s +EEqn Time = 0.000366 s +EEqn assamble = 0.000274 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 213.99 s ClockTime = 215 s +Courant Number mean: 0.003703 max: 0.0235763 +Time = 0.0017225 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21960 + Current mass in system = 1.37508e-09 + Linear momentum = (2.09591e-11 -7.36727e-09 0) + |Linear momentum| = 7.3673e-09 + Linear kinetic energy = 2.11417e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 417.347, 540.2 + Mass transfer phase change = 3.31066e-10 + D10, D32, Dmax (mu) = 62.5539, 86.0034, 178.015 + Liquid penetration 95% mass (m) = 0.0120291 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0538509, Final residual = 2.6648e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0260516, Final residual = 8.72401e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000901829, Final residual = 7.39611e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000555305, Final residual = 5.30951e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000628354, Final residual = 6.36127e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000628331, Final residual = 6.37971e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000895097, Final residual = 6.72742e-08, No Iterations 1 +min/max(T) = 806.269, 2752.94 +GAMG: Solving for p, Initial residual = 0.024247, Final residual = 0.000521224, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.89272e-05, global = 1.59243e-05, cumulative = 0.00753659 +GAMG: Solving for p, Initial residual = 0.000510138, Final residual = 3.87938e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.62249e-05, global = 1.62235e-05, cumulative = 0.00755281 +smoothSolver: Solving for epsilon, Initial residual = 0.000885321, Final residual = 1.14293e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0009581, Final residual = 1.79458e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.101767 s +other Time = 1e-06 s +rho Equations = 0.000189 s +U Equations = 0.001331 s +Y Equations = 0.00208611 s +E Equations = 0.000478 s +p Equations = 0.00178 s +calculate parcels = 147.821 s +chemistry correctThermo = 0.002059 s +turbulence correct = 0.000845 s +combustion correct(in Y) = 0.0927989 s +percentage of chemistry = 91.1876 % +percentage of rho/U/Y/E = 4.0132 % +========Time details of each equation======= +rhoEqn Time = 0.000303 s +rhoEqn assamble = 0.00024 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001329 s +UEqn assamble = 0.000796 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000533 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001432 s +YEqn assamble = 0.000522 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.3e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000362 s +EEqn assamble = 0.000271 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 214.45 s ClockTime = 215 s +Courant Number mean: 0.00376293 max: 0.0236546 +Time = 0.001725 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21960 + Current mass in system = 1.37367e-09 + Linear momentum = (2.10812e-11 -7.35514e-09 0) + |Linear momentum| = 7.35517e-09 + Linear kinetic energy = 2.10935e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 417.548, 540.2 + Mass transfer phase change = 3.32474e-10 + D10, D32, Dmax (mu) = 62.4942, 85.9656, 177.824 + Liquid penetration 95% mass (m) = 0.0120411 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0484087, Final residual = 2.37967e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0248532, Final residual = 8.33925e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000897108, Final residual = 7.36639e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000549998, Final residual = 5.26283e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000623662, Final residual = 6.31451e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000623652, Final residual = 6.33261e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000893392, Final residual = 6.64767e-08, No Iterations 1 +min/max(T) = 806.286, 2752.59 +GAMG: Solving for p, Initial residual = 0.0254496, Final residual = 0.000578778, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.91518e-05, global = 1.59888e-05, cumulative = 0.0075688 +GAMG: Solving for p, Initial residual = 0.000568848, Final residual = 3.90257e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.62351e-05, global = 1.62338e-05, cumulative = 0.00758503 +smoothSolver: Solving for epsilon, Initial residual = 0.000882218, Final residual = 1.13405e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000956042, Final residual = 1.78768e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.087589 s +other Time = 0 s +rho Equations = 0.000161 s +U Equations = 0.001024 s +Y Equations = 0.0023395 s +E Equations = 0.000534 s +p Equations = 0.002085 s +calculate parcels = 148.17 s +chemistry correctThermo = 0.002067 s +turbulence correct = 0.000994 s +combustion correct(in Y) = 0.0782025 s +percentage of chemistry = 89.2835 % +percentage of rho/U/Y/E = 4.63357 % +========Time details of each equation======= +rhoEqn Time = 0.000307 s +rhoEqn assamble = 0.000247 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001022 s +UEqn assamble = 0.000595 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000427 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001725 s +YEqn assamble = 0.000602 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000135 s +YEqn correct boundary = 0 s +EEqn Time = 0.000397 s +EEqn assamble = 0.000296 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000101 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 214.89 s ClockTime = 215 s +Courant Number mean: 0.00382689 max: 0.0236933 +Time = 0.0017275 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21959 + Current mass in system = 1.37225e-09 + Linear momentum = (2.11589e-11 -7.34299e-09 0) + |Linear momentum| = 7.34302e-09 + Linear kinetic energy = 2.10453e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 417.751, 540.2 + Mass transfer phase change = 3.33894e-10 + D10, D32, Dmax (mu) = 62.4933, 85.9314, 177.635 + Liquid penetration 95% mass (m) = 0.0120517 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0367551, Final residual = 1.7934e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.023698, Final residual = 7.97905e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000899686, Final residual = 7.46097e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000546832, Final residual = 5.23492e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000619453, Final residual = 6.27019e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000619431, Final residual = 6.28811e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000892971, Final residual = 6.58315e-08, No Iterations 1 +min/max(T) = 806.306, 2752.26 +GAMG: Solving for p, Initial residual = 0.0268978, Final residual = 0.000615448, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.93518e-05, global = 1.615e-05, cumulative = 0.00760118 +GAMG: Solving for p, Initial residual = 0.000606465, Final residual = 4.63713e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.63692e-05, global = 1.63677e-05, cumulative = 0.00761755 +smoothSolver: Solving for epsilon, Initial residual = 0.000879578, Final residual = 1.1267e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000953096, Final residual = 1.78181e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.080026 s +other Time = 1e-06 s +rho Equations = 0.000177 s +U Equations = 0.001088 s +Y Equations = 0.00276001 s +E Equations = 0.000618 s +p Equations = 0.00217 s +calculate parcels = 148.432 s +chemistry correctThermo = 0.002564 s +turbulence correct = 0.000898 s +combustion correct(in Y) = 0.069542 s +percentage of chemistry = 86.8992 % +percentage of rho/U/Y/E = 5.80188 % +========Time details of each equation======= +rhoEqn Time = 0.000347 s +rhoEqn assamble = 0.000263 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001088 s +UEqn assamble = 0.000655 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000433 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002106 s +YEqn assamble = 0.000716 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000204 s +YEqn correct boundary = 0 s +EEqn Time = 0.000454 s +EEqn assamble = 0.000339 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 215.23 s ClockTime = 216 s +Courant Number mean: 0.00389899 max: 0.0236891 +Time = 0.00173 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21959 + Current mass in system = 1.37084e-09 + Linear momentum = (2.11881e-11 -7.3309e-09 0) + |Linear momentum| = 7.33093e-09 + Linear kinetic energy = 2.09973e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 417.956, 540.2 + Mass transfer phase change = 3.35305e-10 + D10, D32, Dmax (mu) = 62.4332, 85.8929, 177.447 + Liquid penetration 95% mass (m) = 0.0120624 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0263738, Final residual = 1.22464e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0225825, Final residual = 7.64261e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000886265, Final residual = 7.23148e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000544396, Final residual = 5.20951e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000618555, Final residual = 6.26173e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000618531, Final residual = 6.27969e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000892515, Final residual = 6.4929e-08, No Iterations 1 +min/max(T) = 806.328, 2751.95 +GAMG: Solving for p, Initial residual = 0.0283868, Final residual = 0.000614014, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.91426e-05, global = 1.6025e-05, cumulative = 0.00763357 +GAMG: Solving for p, Initial residual = 0.000607001, Final residual = 2.8382e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.62576e-05, global = 1.62565e-05, cumulative = 0.00764983 +smoothSolver: Solving for epsilon, Initial residual = 0.000872547, Final residual = 1.11327e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000947101, Final residual = 1.77161e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.108757 s +other Time = 0 s +rho Equations = 0.000183 s +U Equations = 0.001221 s +Y Equations = 0.00279048 s +E Equations = 0.000712 s +p Equations = 0.002765 s +calculate parcels = 148.775 s +chemistry correctThermo = 0.003056 s +turbulence correct = 0.001121 s +combustion correct(in Y) = 0.0966905 s +percentage of chemistry = 88.9051 % +percentage of rho/U/Y/E = 4.51141 % +========Time details of each equation======= +rhoEqn Time = 0.000362 s +rhoEqn assamble = 0.000283 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00122 s +UEqn assamble = 0.000703 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000517 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002143 s +YEqn assamble = 0.000747 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000256 s +YEqn correct boundary = 0 s +EEqn Time = 0.000532 s +EEqn assamble = 0.000391 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000141 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 215.68 s ClockTime = 216 s +Courant Number mean: 0.00397336 max: 0.0236408 +Time = 0.0017325 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21958 + Current mass in system = 1.36942e-09 + Linear momentum = (2.11734e-11 -7.31881e-09 0) + |Linear momentum| = 7.31884e-09 + Linear kinetic energy = 2.09494e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 418.164, 540.2 + Mass transfer phase change = 3.36719e-10 + D10, D32, Dmax (mu) = 62.4539, 85.8558, 177.26 + Liquid penetration 95% mass (m) = 0.012074 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0268912, Final residual = 1.25307e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0214435, Final residual = 7.27696e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000882348, Final residual = 7.18782e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000543597, Final residual = 5.20371e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00061743, Final residual = 6.25469e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000617403, Final residual = 6.27274e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000891807, Final residual = 6.43709e-08, No Iterations 1 +min/max(T) = 806.35, 2751.68 +GAMG: Solving for p, Initial residual = 0.0296901, Final residual = 0.000557396, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.88243e-05, global = 1.60551e-05, cumulative = 0.00766589 +GAMG: Solving for p, Initial residual = 0.000552226, Final residual = 3.49789e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.62987e-05, global = 1.62976e-05, cumulative = 0.00768218 +smoothSolver: Solving for epsilon, Initial residual = 0.000865594, Final residual = 1.10128e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000940391, Final residual = 1.76079e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102137 s +other Time = 0 s +rho Equations = 0.000185 s +U Equations = 0.001409 s +Y Equations = 0.00213924 s +E Equations = 0.000485 s +p Equations = 0.001746 s +calculate parcels = 149.125 s +chemistry correctThermo = 0.002046 s +turbulence correct = 0.000786 s +combustion correct(in Y) = 0.0931208 s +percentage of chemistry = 91.1724 % +percentage of rho/U/Y/E = 4.12999 % +========Time details of each equation======= +rhoEqn Time = 0.000297 s +rhoEqn assamble = 0.000233 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001408 s +UEqn assamble = 0.000866 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000542 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001468 s +YEqn assamble = 0.000529 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.3e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000365 s +EEqn assamble = 0.00027 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 216.14 s ClockTime = 217 s +Courant Number mean: 0.00404681 max: 0.0235719 +Time = 0.001735 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21958 + Current mass in system = 1.36801e-09 + Linear momentum = (2.11207e-11 -7.30673e-09 0) + |Linear momentum| = 7.30676e-09 + Linear kinetic energy = 2.09016e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 418.375, 540.2 + Mass transfer phase change = 3.38131e-10 + D10, D32, Dmax (mu) = 62.3939, 85.8166, 177.075 + Liquid penetration 95% mass (m) = 0.0120867 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0311192, Final residual = 1.49713e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0203838, Final residual = 6.91122e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000876037, Final residual = 7.11485e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000543668, Final residual = 5.20921e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000617745, Final residual = 6.2656e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000617714, Final residual = 6.28369e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000891731, Final residual = 6.40585e-08, No Iterations 1 +min/max(T) = 806.373, 2751.45 +GAMG: Solving for p, Initial residual = 0.0312244, Final residual = 0.000484264, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.83676e-05, global = 1.5998e-05, cumulative = 0.00769818 +GAMG: Solving for p, Initial residual = 0.000481127, Final residual = 2.91817e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.62775e-05, global = 1.62765e-05, cumulative = 0.00771446 +smoothSolver: Solving for epsilon, Initial residual = 0.000858523, Final residual = 1.08989e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000933216, Final residual = 1.75199e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097778 s +other Time = 0 s +rho Equations = 0.000175 s +U Equations = 0.001282 s +Y Equations = 0.00209005 s +E Equations = 0.000519 s +p Equations = 0.002444 s +calculate parcels = 149.461 s +chemistry correctThermo = 0.002671 s +turbulence correct = 0.00115 s +combustion correct(in Y) = 0.0872399 s +percentage of chemistry = 89.2225 % +percentage of rho/U/Y/E = 4.15845 % +========Time details of each equation======= +rhoEqn Time = 0.000331 s +rhoEqn assamble = 0.000262 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001281 s +UEqn assamble = 0.000783 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000498 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001434 s +YEqn assamble = 0.000521 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000401 s +EEqn assamble = 0.000304 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.7e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 216.57 s ClockTime = 217 s +Courant Number mean: 0.0041184 max: 0.0234844 +Time = 0.0017375 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21958 + Current mass in system = 1.3666e-09 + Linear momentum = (2.10346e-11 -7.29464e-09 0) + |Linear momentum| = 7.29467e-09 + Linear kinetic energy = 2.08537e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 418.589, 540.2 + Mass transfer phase change = 3.39545e-10 + D10, D32, Dmax (mu) = 62.3342, 85.777, 176.891 + Liquid penetration 95% mass (m) = 0.0120986 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0338587, Final residual = 1.66539e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0193609, Final residual = 6.55076e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000873667, Final residual = 7.06705e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000544097, Final residual = 5.22108e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000618141, Final residual = 6.27743e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000618119, Final residual = 6.29562e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000891854, Final residual = 6.36949e-08, No Iterations 1 +min/max(T) = 806.396, 2751.27 +GAMG: Solving for p, Initial residual = 0.032774, Final residual = 0.000445283, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.81046e-05, global = 1.59852e-05, cumulative = 0.00773044 +GAMG: Solving for p, Initial residual = 0.00044299, Final residual = 2.06816e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.63011e-05, global = 1.63004e-05, cumulative = 0.00774674 +smoothSolver: Solving for epsilon, Initial residual = 0.000850554, Final residual = 1.07714e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000925599, Final residual = 1.74096e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.105703 s +other Time = 0 s +rho Equations = 0.000183 s +U Equations = 0.001355 s +Y Equations = 0.0024206 s +E Equations = 0.000602 s +p Equations = 0.002202 s +calculate parcels = 149.825 s +chemistry correctThermo = 0.002825 s +turbulence correct = 0.000991 s +combustion correct(in Y) = 0.0949194 s +percentage of chemistry = 89.7982 % +percentage of rho/U/Y/E = 4.31454 % +========Time details of each equation======= +rhoEqn Time = 0.000323 s +rhoEqn assamble = 0.000254 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001355 s +UEqn assamble = 0.000823 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000532 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001755 s +YEqn assamble = 0.000617 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000166 s +YEqn correct boundary = 0 s +EEqn Time = 0.000444 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 217.04 s ClockTime = 218 s +Courant Number mean: 0.00418736 max: 0.0233282 +Time = 0.00174 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21958 + Current mass in system = 1.36518e-09 + Linear momentum = (2.09218e-11 -7.2825e-09 0) + |Linear momentum| = 7.28253e-09 + Linear kinetic energy = 2.08056e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 418.807, 540.2 + Mass transfer phase change = 3.40963e-10 + D10, D32, Dmax (mu) = 62.2751, 85.7369, 176.706 + Liquid penetration 95% mass (m) = 0.0121112 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.033389, Final residual = 1.66707e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0184774, Final residual = 6.22266e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000869738, Final residual = 6.97499e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000544161, Final residual = 5.22777e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000617761, Final residual = 6.27958e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000617746, Final residual = 6.2978e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000890482, Final residual = 6.31133e-08, No Iterations 1 +min/max(T) = 806.419, 2751.1 +GAMG: Solving for p, Initial residual = 0.0344522, Final residual = 0.000481771, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.81451e-05, global = 1.5984e-05, cumulative = 0.00776273 +GAMG: Solving for p, Initial residual = 0.000479338, Final residual = 2.65808e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.63377e-05, global = 1.63367e-05, cumulative = 0.00777906 +smoothSolver: Solving for epsilon, Initial residual = 0.000840963, Final residual = 1.06241e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000916978, Final residual = 1.72767e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.076275 s +other Time = 1e-06 s +rho Equations = 0.000177 s +U Equations = 0.001061 s +Y Equations = 0.0025708 s +E Equations = 0.000489 s +p Equations = 0.001908 s +calculate parcels = 150.15 s +chemistry correctThermo = 0.001942 s +turbulence correct = 0.00083 s +combustion correct(in Y) = 0.0671062 s +percentage of chemistry = 87.9793 % +percentage of rho/U/Y/E = 5.63461 % +========Time details of each equation======= +rhoEqn Time = 0.000302 s +rhoEqn assamble = 0.000241 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001059 s +UEqn assamble = 0.000636 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000423 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001911 s +YEqn assamble = 0.000585 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000318 s +YEqn correct boundary = 0 s +EEqn Time = 0.000367 s +EEqn assamble = 0.000275 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 217.44 s ClockTime = 218 s +Courant Number mean: 0.00425341 max: 0.0231364 +Time = 0.0017425 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21958 + Current mass in system = 1.36376e-09 + Linear momentum = (2.07882e-11 -7.27028e-09 0) + |Linear momentum| = 7.27031e-09 + Linear kinetic energy = 2.07572e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 419.028, 540.2 + Mass transfer phase change = 3.42384e-10 + D10, D32, Dmax (mu) = 62.2171, 85.6961, 176.521 + Liquid penetration 95% mass (m) = 0.0121227 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0296747, Final residual = 1.492e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0177446, Final residual = 5.94301e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000866918, Final residual = 6.91242e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000543239, Final residual = 5.22995e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00061692, Final residual = 6.27584e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000616932, Final residual = 6.29406e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000889646, Final residual = 6.28095e-08, No Iterations 1 +min/max(T) = 806.443, 2750.94 +GAMG: Solving for p, Initial residual = 0.0362358, Final residual = 0.000529292, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.82708e-05, global = 1.60095e-05, cumulative = 0.00779507 +GAMG: Solving for p, Initial residual = 0.000527256, Final residual = 3.26752e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.63875e-05, global = 1.63864e-05, cumulative = 0.00781146 +smoothSolver: Solving for epsilon, Initial residual = 0.000830549, Final residual = 1.04455e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00090751, Final residual = 1.71045e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100741 s +other Time = 0 s +rho Equations = 0.000173 s +U Equations = 0.001198 s +Y Equations = 0.00206763 s +E Equations = 0.000482 s +p Equations = 0.00177 s +calculate parcels = 150.435 s +chemistry correctThermo = 0.002021 s +turbulence correct = 0.000803 s +combustion correct(in Y) = 0.0920314 s +percentage of chemistry = 91.3544 % +percentage of rho/U/Y/E = 3.89179 % +========Time details of each equation======= +rhoEqn Time = 0.000288 s +rhoEqn assamble = 0.000226 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001196 s +UEqn assamble = 0.000679 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000517 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001419 s +YEqn assamble = 0.000509 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000365 s +EEqn assamble = 0.000273 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 217.83 s ClockTime = 218 s +Courant Number mean: 0.00431604 max: 0.0229184 +Time = 0.001745 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21958 + Current mass in system = 1.36233e-09 + Linear momentum = (2.06406e-11 -7.25797e-09 0) + |Linear momentum| = 7.258e-09 + Linear kinetic energy = 2.07083e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 419.252, 540.2 + Mass transfer phase change = 3.43811e-10 + D10, D32, Dmax (mu) = 62.1592, 85.6545, 176.336 + Liquid penetration 95% mass (m) = 0.0121337 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0237449, Final residual = 1.19751e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0170523, Final residual = 5.69369e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000862936, Final residual = 6.8244e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000541025, Final residual = 5.21689e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000615017, Final residual = 6.25165e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000615041, Final residual = 6.26983e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00088753, Final residual = 6.23887e-08, No Iterations 1 +min/max(T) = 806.467, 2750.76 +GAMG: Solving for p, Initial residual = 0.0382255, Final residual = 0.000568959, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.83748e-05, global = 1.60644e-05, cumulative = 0.00782753 +GAMG: Solving for p, Initial residual = 0.000567202, Final residual = 3.39144e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.64435e-05, global = 1.64424e-05, cumulative = 0.00784397 +smoothSolver: Solving for epsilon, Initial residual = 0.000819805, Final residual = 1.02686e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000897531, Final residual = 1.69094e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.109536 s +other Time = 1e-06 s +rho Equations = 0.000181 s +U Equations = 0.001239 s +Y Equations = 0.00211988 s +E Equations = 0.000538 s +p Equations = 0.002279 s +calculate parcels = 150.791 s +chemistry correctThermo = 0.002242 s +turbulence correct = 0.000976 s +combustion correct(in Y) = 0.0997571 s +percentage of chemistry = 91.0724 % +percentage of rho/U/Y/E = 3.72287 % +========Time details of each equation======= +rhoEqn Time = 0.000351 s +rhoEqn assamble = 0.000281 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001238 s +UEqn assamble = 0.000737 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000501 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001467 s +YEqn assamble = 0.000527 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000101 s +YEqn correct boundary = 0 s +EEqn Time = 0.000416 s +EEqn assamble = 0.000315 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000101 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 218.29 s ClockTime = 219 s +Courant Number mean: 0.004374 max: 0.0227216 +Time = 0.0017475 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21958 + Current mass in system = 1.3609e-09 + Linear momentum = (2.04816e-11 -7.24556e-09 0) + |Linear momentum| = 7.24559e-09 + Linear kinetic energy = 2.0659e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 419.479, 540.2 + Mass transfer phase change = 3.45242e-10 + D10, D32, Dmax (mu) = 62.101, 85.6122, 176.151 + Liquid penetration 95% mass (m) = 0.0121446 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0179702, Final residual = 8.83427e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0164189, Final residual = 5.47372e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000857819, Final residual = 6.73418e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000537273, Final residual = 5.18452e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000611261, Final residual = 6.2009e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000611283, Final residual = 6.21907e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000884989, Final residual = 6.19864e-08, No Iterations 1 +min/max(T) = 806.491, 2750.55 +GAMG: Solving for p, Initial residual = 0.0407497, Final residual = 0.000586114, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.84175e-05, global = 1.61354e-05, cumulative = 0.0078601 +GAMG: Solving for p, Initial residual = 0.000584933, Final residual = 3.61557e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.65e-05, global = 1.64988e-05, cumulative = 0.0078766 +smoothSolver: Solving for epsilon, Initial residual = 0.000809327, Final residual = 1.00999e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000887277, Final residual = 1.66844e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.101743 s +other Time = 1e-06 s +rho Equations = 0.000164 s +U Equations = 0.001059 s +Y Equations = 0.00263438 s +E Equations = 0.000532 s +p Equations = 0.002366 s +calculate parcels = 151.153 s +chemistry correctThermo = 0.002039 s +turbulence correct = 0.001057 s +combustion correct(in Y) = 0.0916336 s +percentage of chemistry = 90.0638 % +percentage of rho/U/Y/E = 4.31418 % +========Time details of each equation======= +rhoEqn Time = 0.000314 s +rhoEqn assamble = 0.000245 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001058 s +UEqn assamble = 0.000644 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000414 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002095 s +YEqn assamble = 0.000732 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000177 s +YEqn correct boundary = 0 s +EEqn Time = 0.000404 s +EEqn assamble = 0.000307 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.7e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 218.76 s ClockTime = 219 s +Courant Number mean: 0.00443532 max: 0.0224358 +Time = 0.00175 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21958 + Current mass in system = 1.35946e-09 + Linear momentum = (2.0316e-11 -7.23307e-09 0) + |Linear momentum| = 7.2331e-09 + Linear kinetic energy = 2.06094e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 419.71, 540.2 + Mass transfer phase change = 3.46679e-10 + D10, D32, Dmax (mu) = 62.0421, 85.5692, 175.964 + Liquid penetration 95% mass (m) = 0.0121567 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0172507, Final residual = 8.58401e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0158242, Final residual = 5.27989e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00085368, Final residual = 6.63402e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000532793, Final residual = 5.13427e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000606477, Final residual = 6.12969e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000606501, Final residual = 6.14767e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000883726, Final residual = 6.13467e-08, No Iterations 1 +min/max(T) = 806.515, 2750.29 +GAMG: Solving for p, Initial residual = 0.0440934, Final residual = 0.000565511, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.83437e-05, global = 1.62258e-05, cumulative = 0.00789283 +GAMG: Solving for p, Initial residual = 0.000564923, Final residual = 3.23931e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.65538e-05, global = 1.65528e-05, cumulative = 0.00790938 +smoothSolver: Solving for epsilon, Initial residual = 0.000798103, Final residual = 9.93053e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000877045, Final residual = 1.64355e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.111031 s +other Time = 0 s +rho Equations = 0.000184 s +U Equations = 0.001294 s +Y Equations = 0.00241792 s +E Equations = 0.000597 s +p Equations = 0.002237 s +calculate parcels = 151.485 s +chemistry correctThermo = 0.002862 s +turbulence correct = 0.001181 s +combustion correct(in Y) = 0.100029 s +percentage of chemistry = 90.0911 % +percentage of rho/U/Y/E = 4.04655 % +========Time details of each equation======= +rhoEqn Time = 0.000323 s +rhoEqn assamble = 0.000253 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001293 s +UEqn assamble = 0.000793 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.0005 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001765 s +YEqn assamble = 0.000643 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000166 s +YEqn correct boundary = 0 s +EEqn Time = 0.000444 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 219.2 s ClockTime = 220 s +Courant Number mean: 0.00449561 max: 0.0220847 +Time = 0.0017525 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21958 + Current mass in system = 1.35802e-09 + Linear momentum = (2.01485e-11 -7.22051e-09 0) + |Linear momentum| = 7.22054e-09 + Linear kinetic energy = 2.05594e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 419.945, 540.2 + Mass transfer phase change = 3.48119e-10 + D10, D32, Dmax (mu) = 61.9828, 85.5254, 175.778 + Liquid penetration 95% mass (m) = 0.0121671 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0201377, Final residual = 1.03305e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.015287, Final residual = 5.1144e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000849905, Final residual = 6.55817e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000527709, Final residual = 5.07611e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000600754, Final residual = 6.05151e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000600761, Final residual = 6.06952e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000886548, Final residual = 6.1001e-08, No Iterations 1 +min/max(T) = 806.539, 2750 +GAMG: Solving for p, Initial residual = 0.0476187, Final residual = 0.00051868, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.81845e-05, global = 1.63202e-05, cumulative = 0.0079257 +GAMG: Solving for p, Initial residual = 0.000520798, Final residual = 2.80043e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.66054e-05, global = 1.66046e-05, cumulative = 0.00794231 +smoothSolver: Solving for epsilon, Initial residual = 0.000786584, Final residual = 9.74149e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000867073, Final residual = 1.61676e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.108161 s +other Time = 1e-06 s +rho Equations = 0.000194 s +U Equations = 0.001194 s +Y Equations = 0.00240328 s +E Equations = 0.000636 s +p Equations = 0.002304 s +calculate parcels = 151.815 s +chemistry correctThermo = 0.00285 s +turbulence correct = 0.001039 s +combustion correct(in Y) = 0.0973287 s +percentage of chemistry = 89.985 % +percentage of rho/U/Y/E = 4.09323 % +========Time details of each equation======= +rhoEqn Time = 0.000354 s +rhoEqn assamble = 0.000279 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001193 s +UEqn assamble = 0.000693 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.0005 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001752 s +YEqn assamble = 0.00065 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00016 s +YEqn correct boundary = 0 s +EEqn Time = 0.000478 s +EEqn assamble = 0.000345 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000133 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 219.64 s ClockTime = 220 s +Courant Number mean: 0.00454636 max: 0.0217043 +Time = 0.001755 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21957 + Current mass in system = 1.35658e-09 + Linear momentum = (1.99844e-11 -7.20789e-09 0) + |Linear momentum| = 7.20792e-09 + Linear kinetic energy = 2.05092e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 420.182, 540.2 + Mass transfer phase change = 3.49566e-10 + D10, D32, Dmax (mu) = 61.9893, 85.4818, 175.591 + Liquid penetration 95% mass (m) = 0.012179 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0234664, Final residual = 1.20892e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0148511, Final residual = 4.98647e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000846512, Final residual = 6.49026e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000522913, Final residual = 5.01238e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000594859, Final residual = 5.96612e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000594869, Final residual = 5.98383e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000887981, Final residual = 6.06512e-08, No Iterations 1 +min/max(T) = 806.561, 2749.67 +GAMG: Solving for p, Initial residual = 0.051174, Final residual = 0.000480105, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.80562e-05, global = 1.6421e-05, cumulative = 0.00795873 +GAMG: Solving for p, Initial residual = 0.000484719, Final residual = 2.24817e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.6672e-05, global = 1.66714e-05, cumulative = 0.0079754 +smoothSolver: Solving for epsilon, Initial residual = 0.000776338, Final residual = 9.56174e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00085812, Final residual = 1.58938e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.076791 s +other Time = 0 s +rho Equations = 0.000169 s +U Equations = 0.001325 s +Y Equations = 0.00214579 s +E Equations = 0.000491 s +p Equations = 0.001883 s +calculate parcels = 152.109 s +chemistry correctThermo = 0.001997 s +turbulence correct = 0.000993 s +combustion correct(in Y) = 0.0675942 s +percentage of chemistry = 88.0236 % +percentage of rho/U/Y/E = 5.37927 % +========Time details of each equation======= +rhoEqn Time = 0.000296 s +rhoEqn assamble = 0.000237 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001323 s +UEqn assamble = 0.000847 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000476 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001554 s +YEqn assamble = 0.000558 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000128 s +YEqn correct boundary = 0 s +EEqn Time = 0.000369 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 220.01 s ClockTime = 221 s +Courant Number mean: 0.00458817 max: 0.0212718 +Time = 0.0017575 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21957 + Current mass in system = 1.35513e-09 + Linear momentum = (1.98287e-11 -7.19522e-09 0) + |Linear momentum| = 7.19525e-09 + Linear kinetic energy = 2.04587e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 420.423, 540.2 + Mass transfer phase change = 3.51014e-10 + D10, D32, Dmax (mu) = 61.9292, 85.4364, 175.404 + Liquid penetration 95% mass (m) = 0.0121898 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0256178, Final residual = 1.315e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.014636, Final residual = 4.93267e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000840705, Final residual = 6.39506e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000517943, Final residual = 4.93578e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000589248, Final residual = 5.87178e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000589249, Final residual = 5.88915e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000887472, Final residual = 6.00603e-08, No Iterations 1 +min/max(T) = 806.58, 2749.31 +GAMG: Solving for p, Initial residual = 0.0546671, Final residual = 0.000505877, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.80782e-05, global = 1.64793e-05, cumulative = 0.00799188 +GAMG: Solving for p, Initial residual = 0.000513451, Final residual = 3.23695e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.66984e-05, global = 1.66977e-05, cumulative = 0.00800857 +smoothSolver: Solving for epsilon, Initial residual = 0.000768455, Final residual = 9.37255e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000850368, Final residual = 1.56371e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09407 s +other Time = 1e-06 s +rho Equations = 0.000167 s +U Equations = 0.000971 s +Y Equations = 0.00240675 s +E Equations = 0.000595 s +p Equations = 0.002201 s +calculate parcels = 152.432 s +chemistry correctThermo = 0.00291 s +turbulence correct = 0.000958 s +combustion correct(in Y) = 0.0836803 s +percentage of chemistry = 88.9553 % +percentage of rho/U/Y/E = 4.40071 % +========Time details of each equation======= +rhoEqn Time = 0.000313 s +rhoEqn assamble = 0.000238 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00097 s +UEqn assamble = 0.000562 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000408 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001857 s +YEqn assamble = 0.000645 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000237 s +YEqn correct boundary = 0 s +EEqn Time = 0.000438 s +EEqn assamble = 0.000327 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 220.43 s ClockTime = 221 s +Courant Number mean: 0.00462214 max: 0.0208075 +Time = 0.00176 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21957 + Current mass in system = 1.35368e-09 + Linear momentum = (1.96908e-11 -7.18252e-09 0) + |Linear momentum| = 7.18255e-09 + Linear kinetic energy = 2.04081e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 420.667, 540.2 + Mass transfer phase change = 3.52467e-10 + D10, D32, Dmax (mu) = 61.8684, 85.3903, 175.216 + Liquid penetration 95% mass (m) = 0.0122014 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0256485, Final residual = 1.3068e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0148469, Final residual = 5.02753e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000836628, Final residual = 6.31177e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000513245, Final residual = 4.85308e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000584014, Final residual = 5.77145e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00058402, Final residual = 5.78867e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000885476, Final residual = 5.94996e-08, No Iterations 1 +min/max(T) = 806.592, 2748.93 +GAMG: Solving for p, Initial residual = 0.058, Final residual = 0.000569718, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.82092e-05, global = 1.65425e-05, cumulative = 0.00802512 +GAMG: Solving for p, Initial residual = 0.000581053, Final residual = 3.60643e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.67397e-05, global = 1.6739e-05, cumulative = 0.00804186 +smoothSolver: Solving for epsilon, Initial residual = 0.000761408, Final residual = 9.19777e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000842769, Final residual = 1.53905e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.118575 s +other Time = 0 s +rho Equations = 0.000218 s +U Equations = 0.001659 s +Y Equations = 0.00259567 s +E Equations = 0.000604 s +p Equations = 0.002345 s +calculate parcels = 152.783 s +chemistry correctThermo = 0.002862 s +turbulence correct = 0.000992 s +combustion correct(in Y) = 0.107081 s +percentage of chemistry = 90.3068 % +percentage of rho/U/Y/E = 4.2814 % +========Time details of each equation======= +rhoEqn Time = 0.000373 s +rhoEqn assamble = 0.000293 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001657 s +UEqn assamble = 0.001014 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000643 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001753 s +YEqn assamble = 0.00066 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000447 s +EEqn assamble = 0.000333 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 220.9 s ClockTime = 221 s +Courant Number mean: 0.00465112 max: 0.0203273 +Time = 0.0017625 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21957 + Current mass in system = 1.35222e-09 + Linear momentum = (1.95777e-11 -7.16979e-09 0) + |Linear momentum| = 7.16981e-09 + Linear kinetic energy = 2.03574e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 420.914, 540.2 + Mass transfer phase change = 3.53922e-10 + D10, D32, Dmax (mu) = 61.8078, 85.3438, 175.029 + Liquid penetration 95% mass (m) = 0.0122133 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0233033, Final residual = 1.18176e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0157536, Final residual = 5.343e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000831548, Final residual = 6.20817e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000508668, Final residual = 4.76465e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000578905, Final residual = 5.66407e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000578899, Final residual = 5.68096e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000880979, Final residual = 5.89117e-08, No Iterations 1 +min/max(T) = 806.591, 2748.54 +GAMG: Solving for p, Initial residual = 0.0611635, Final residual = 0.000629763, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.83008e-05, global = 1.65893e-05, cumulative = 0.00805845 +GAMG: Solving for p, Initial residual = 0.000643098, Final residual = 4.28887e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.67737e-05, global = 1.67729e-05, cumulative = 0.00807522 +smoothSolver: Solving for epsilon, Initial residual = 0.000754901, Final residual = 9.04006e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000834986, Final residual = 1.51408e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.110417 s +other Time = 0 s +rho Equations = 0.000178 s +U Equations = 0.00126 s +Y Equations = 0.00246992 s +E Equations = 0.000612 s +p Equations = 0.002257 s +calculate parcels = 153.132 s +chemistry correctThermo = 0.002888 s +turbulence correct = 0.001026 s +combustion correct(in Y) = 0.0995171 s +percentage of chemistry = 90.1284 % +percentage of rho/U/Y/E = 4.0935 % +========Time details of each equation======= +rhoEqn Time = 0.000325 s +rhoEqn assamble = 0.00026 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001259 s +UEqn assamble = 0.00075 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000509 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00182 s +YEqn assamble = 0.000676 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000181 s +YEqn correct boundary = 0 s +EEqn Time = 0.000455 s +EEqn assamble = 0.000342 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 221.36 s ClockTime = 222 s +Courant Number mean: 0.00467862 max: 0.0198174 +Time = 0.001765 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21957 + Current mass in system = 1.35076e-09 + Linear momentum = (1.94918e-11 -7.15704e-09 0) + |Linear momentum| = 7.15706e-09 + Linear kinetic energy = 2.03067e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 421.165, 540.2 + Mass transfer phase change = 3.5538e-10 + D10, D32, Dmax (mu) = 61.7467, 85.2969, 174.842 + Liquid penetration 95% mass (m) = 0.0122244 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0190753, Final residual = 9.69965e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0171952, Final residual = 5.7567e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000827726, Final residual = 6.10945e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000504359, Final residual = 4.66694e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000573925, Final residual = 5.54738e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000573915, Final residual = 5.56382e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000874574, Final residual = 5.80884e-08, No Iterations 1 +min/max(T) = 806.577, 2748.14 +GAMG: Solving for p, Initial residual = 0.0635399, Final residual = 0.000677458, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.83549e-05, global = 1.66271e-05, cumulative = 0.00809185 +GAMG: Solving for p, Initial residual = 0.000682306, Final residual = 4.89024e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.6801e-05, global = 1.68002e-05, cumulative = 0.00810865 +smoothSolver: Solving for epsilon, Initial residual = 0.000748344, Final residual = 8.88322e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000826987, Final residual = 1.48939e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.096843 s +other Time = 0 s +rho Equations = 0.000185 s +U Equations = 0.001206 s +Y Equations = 0.0025034 s +E Equations = 0.000612 s +p Equations = 0.002372 s +calculate parcels = 153.517 s +chemistry correctThermo = 0.002874 s +turbulence correct = 0.000993 s +combustion correct(in Y) = 0.0858886 s +percentage of chemistry = 88.6885 % +percentage of rho/U/Y/E = 4.6533 % +========Time details of each equation======= +rhoEqn Time = 0.000344 s +rhoEqn assamble = 0.00027 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001204 s +UEqn assamble = 0.000706 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000498 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001834 s +YEqn assamble = 0.000635 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000177 s +YEqn correct boundary = 0 s +EEqn Time = 0.000449 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 221.84 s ClockTime = 222 s +Courant Number mean: 0.00470563 max: 0.0192777 +Time = 0.0017675 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21957 + Current mass in system = 1.3493e-09 + Linear momentum = (1.94312e-11 -7.14429e-09 0) + |Linear momentum| = 7.14431e-09 + Linear kinetic energy = 2.0256e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 421.418, 540.2 + Mass transfer phase change = 3.56839e-10 + D10, D32, Dmax (mu) = 61.6854, 85.2497, 175.236 + Liquid penetration 95% mass (m) = 0.0122356 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0144096, Final residual = 7.26841e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0187488, Final residual = 6.2111e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000823896, Final residual = 6.00529e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000499817, Final residual = 4.56836e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000568429, Final residual = 5.42882e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000568416, Final residual = 5.44484e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000866474, Final residual = 5.72917e-08, No Iterations 1 +min/max(T) = 806.566, 2747.74 +GAMG: Solving for p, Initial residual = 0.0640902, Final residual = 0.000663598, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.83003e-05, global = 1.66485e-05, cumulative = 0.00812529 +GAMG: Solving for p, Initial residual = 0.000659638, Final residual = 3.20185e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.68219e-05, global = 1.68213e-05, cumulative = 0.00814212 +smoothSolver: Solving for epsilon, Initial residual = 0.000743392, Final residual = 8.75461e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000819895, Final residual = 1.46667e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.07851 s +other Time = 0 s +rho Equations = 0.000189 s +U Equations = 0.001325 s +Y Equations = 0.00212958 s +E Equations = 0.000521 s +p Equations = 0.001891 s +calculate parcels = 153.867 s +chemistry correctThermo = 0.001982 s +turbulence correct = 0.000861 s +combustion correct(in Y) = 0.0693774 s +percentage of chemistry = 88.3676 % +percentage of rho/U/Y/E = 5.30453 % +========Time details of each equation======= +rhoEqn Time = 0.000319 s +rhoEqn assamble = 0.000256 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001324 s +UEqn assamble = 0.000667 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000657 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001527 s +YEqn assamble = 0.000523 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000121 s +YEqn correct boundary = 0 s +EEqn Time = 0.000396 s +EEqn assamble = 0.000295 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000101 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 222.27 s ClockTime = 223 s +Courant Number mean: 0.00473554 max: 0.0187054 +Time = 0.00177 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21957 + Current mass in system = 1.34784e-09 + Linear momentum = (1.93921e-11 -7.13155e-09 0) + |Linear momentum| = 7.13157e-09 + Linear kinetic energy = 2.02053e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 421.674, 540.2 + Mass transfer phase change = 3.583e-10 + D10, D32, Dmax (mu) = 61.624, 85.2023, 175.71 + Liquid penetration 95% mass (m) = 0.0122469 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0130691, Final residual = 6.18423e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0204066, Final residual = 6.71976e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000820349, Final residual = 5.86892e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000495721, Final residual = 4.46441e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000563196, Final residual = 5.30638e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000563176, Final residual = 5.32194e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000858158, Final residual = 5.63641e-08, No Iterations 1 +min/max(T) = 806.559, 2747.36 +GAMG: Solving for p, Initial residual = 0.0633505, Final residual = 0.000604574, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.81583e-05, global = 1.66751e-05, cumulative = 0.00815879 +GAMG: Solving for p, Initial residual = 0.00059766, Final residual = 3.40872e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.68363e-05, global = 1.68357e-05, cumulative = 0.00817563 +smoothSolver: Solving for epsilon, Initial residual = 0.000739659, Final residual = 8.62638e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000813259, Final residual = 1.44508e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.108883 s +other Time = 0 s +rho Equations = 0.000178 s +U Equations = 0.001248 s +Y Equations = 0.00210144 s +E Equations = 0.000479 s +p Equations = 0.002279 s +calculate parcels = 154.161 s +chemistry correctThermo = 0.002034 s +turbulence correct = 0.001043 s +combustion correct(in Y) = 0.0993136 s +percentage of chemistry = 91.2113 % +percentage of rho/U/Y/E = 3.67959 % +========Time details of each equation======= +rhoEqn Time = 0.000331 s +rhoEqn assamble = 0.000264 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001247 s +UEqn assamble = 0.000749 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000498 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001459 s +YEqn assamble = 0.00053 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.4e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000362 s +EEqn assamble = 0.000271 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 222.67 s ClockTime = 223 s +Courant Number mean: 0.00477144 max: 0.0182391 +Time = 0.0017725 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21957 + Current mass in system = 1.34638e-09 + Linear momentum = (1.93676e-11 -7.11882e-09 0) + |Linear momentum| = 7.11885e-09 + Linear kinetic energy = 2.01548e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 421.934, 540.2 + Mass transfer phase change = 3.59761e-10 + D10, D32, Dmax (mu) = 61.5626, 85.1547, 176.164 + Liquid penetration 95% mass (m) = 0.0122575 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0136628, Final residual = 6.11255e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.022132, Final residual = 7.27841e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000817376, Final residual = 5.7518e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000491375, Final residual = 4.35685e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000557409, Final residual = 5.1818e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000557387, Final residual = 5.19691e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000850322, Final residual = 5.56037e-08, No Iterations 1 +min/max(T) = 806.56, 2747 +GAMG: Solving for p, Initial residual = 0.0622945, Final residual = 0.000532756, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.80174e-05, global = 1.66919e-05, cumulative = 0.00819232 +GAMG: Solving for p, Initial residual = 0.000522399, Final residual = 2.42419e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.68477e-05, global = 1.68472e-05, cumulative = 0.00820917 +smoothSolver: Solving for epsilon, Initial residual = 0.000736657, Final residual = 8.52245e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000806434, Final residual = 1.42304e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.08764 s +other Time = 1e-06 s +rho Equations = 0.000196 s +U Equations = 0.001322 s +Y Equations = 0.00208071 s +E Equations = 0.000479 s +p Equations = 0.002491 s +calculate parcels = 154.508 s +chemistry correctThermo = 0.002463 s +turbulence correct = 0.001218 s +combustion correct(in Y) = 0.0771883 s +percentage of chemistry = 88.0743 % +percentage of rho/U/Y/E = 4.65279 % +========Time details of each equation======= +rhoEqn Time = 0.00036 s +rhoEqn assamble = 0.00028 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001321 s +UEqn assamble = 0.000764 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000557 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001377 s +YEqn assamble = 0.000509 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 6.1e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000359 s +EEqn assamble = 0.000268 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 223.1 s ClockTime = 224 s +Courant Number mean: 0.00480709 max: 0.0178203 +Time = 0.001775 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21957 + Current mass in system = 1.34492e-09 + Linear momentum = (1.93518e-11 -7.10612e-09 0) + |Linear momentum| = 7.10614e-09 + Linear kinetic energy = 2.01044e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 422.197, 540.2 + Mass transfer phase change = 3.61224e-10 + D10, D32, Dmax (mu) = 61.5011, 85.107, 176.544 + Liquid penetration 95% mass (m) = 0.0122689 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0142558, Final residual = 6.29783e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0239293, Final residual = 7.88677e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000813761, Final residual = 5.63958e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000486945, Final residual = 4.24666e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000551568, Final residual = 5.05598e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000551542, Final residual = 5.07063e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000844969, Final residual = 5.50966e-08, No Iterations 1 +min/max(T) = 806.57, 2746.64 +GAMG: Solving for p, Initial residual = 0.0606091, Final residual = 0.000498096, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.79526e-05, global = 1.67106e-05, cumulative = 0.00822588 +GAMG: Solving for p, Initial residual = 0.00048405, Final residual = 2.84247e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.68589e-05, global = 1.68583e-05, cumulative = 0.00824273 +smoothSolver: Solving for epsilon, Initial residual = 0.000734398, Final residual = 8.4281e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00080066, Final residual = 1.40361e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.086752 s +other Time = 0 s +rho Equations = 0.000188 s +U Equations = 0.001285 s +Y Equations = 0.00208837 s +E Equations = 0.000482 s +p Equations = 0.001803 s +calculate parcels = 154.87 s +chemistry correctThermo = 0.002016 s +turbulence correct = 0.000805 s +combustion correct(in Y) = 0.0778856 s +percentage of chemistry = 89.7796 % +percentage of rho/U/Y/E = 4.66084 % +========Time details of each equation======= +rhoEqn Time = 0.000306 s +rhoEqn assamble = 0.000244 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001284 s +UEqn assamble = 0.000774 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00051 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001416 s +YEqn assamble = 0.00051 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.4e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000367 s +EEqn assamble = 0.000274 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 223.55 s ClockTime = 224 s +Courant Number mean: 0.00483909 max: 0.0173771 +Time = 0.0017775 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21957 + Current mass in system = 1.34346e-09 + Linear momentum = (1.93423e-11 -7.09343e-09 0) + |Linear momentum| = 7.09346e-09 + Linear kinetic energy = 2.00541e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 422.463, 540.2 + Mass transfer phase change = 3.62688e-10 + D10, D32, Dmax (mu) = 61.4394, 85.0591, 177.017 + Liquid penetration 95% mass (m) = 0.0122823 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0141794, Final residual = 6.43383e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0257665, Final residual = 8.55093e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000810676, Final residual = 5.55668e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000482053, Final residual = 4.13143e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0005453, Final residual = 4.92909e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000545273, Final residual = 4.94343e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000839164, Final residual = 5.46194e-08, No Iterations 1 +min/max(T) = 806.59, 2746.3 +GAMG: Solving for p, Initial residual = 0.0585162, Final residual = 0.000469075, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.79111e-05, global = 1.67362e-05, cumulative = 0.00825947 +GAMG: Solving for p, Initial residual = 0.000452054, Final residual = 2.73401e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.68696e-05, global = 1.6869e-05, cumulative = 0.00827634 +smoothSolver: Solving for epsilon, Initial residual = 0.000733078, Final residual = 8.33977e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000795982, Final residual = 1.38626e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.110591 s +other Time = 0 s +rho Equations = 0.000178 s +U Equations = 0.001186 s +Y Equations = 0.0024924 s +E Equations = 0.000606 s +p Equations = 0.002424 s +calculate parcels = 155.193 s +chemistry correctThermo = 0.00288 s +turbulence correct = 0.001012 s +combustion correct(in Y) = 0.0996136 s +percentage of chemistry = 90.0739 % +percentage of rho/U/Y/E = 4.03505 % +========Time details of each equation======= +rhoEqn Time = 0.000336 s +rhoEqn assamble = 0.000266 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001186 s +UEqn assamble = 0.000685 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000501 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001846 s +YEqn assamble = 0.000663 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000197 s +YEqn correct boundary = 0 s +EEqn Time = 0.000451 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 223.99 s ClockTime = 225 s +Courant Number mean: 0.00486659 max: 0.0169064 +Time = 0.00178 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21957 + Current mass in system = 1.34199e-09 + Linear momentum = (1.93427e-11 -7.08077e-09 0) + |Linear momentum| = 7.0808e-09 + Linear kinetic energy = 2.0004e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 422.732, 540.2 + Mass transfer phase change = 3.64152e-10 + D10, D32, Dmax (mu) = 61.3778, 85.0113, 177.473 + Liquid penetration 95% mass (m) = 0.0122928 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0139437, Final residual = 6.66298e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0276134, Final residual = 9.26178e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000807335, Final residual = 5.46733e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000476505, Final residual = 4.00914e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000538685, Final residual = 4.79624e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000538662, Final residual = 4.81009e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000832767, Final residual = 5.40448e-08, No Iterations 1 +min/max(T) = 806.62, 2745.96 +GAMG: Solving for p, Initial residual = 0.056367, Final residual = 0.000444651, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.78836e-05, global = 1.67611e-05, cumulative = 0.0082931 +GAMG: Solving for p, Initial residual = 0.000426479, Final residual = 2.55029e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.68814e-05, global = 1.68808e-05, cumulative = 0.00830998 +smoothSolver: Solving for epsilon, Initial residual = 0.000731937, Final residual = 8.25876e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000791752, Final residual = 1.37128e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.11015 s +other Time = 0 s +rho Equations = 0.000157 s +U Equations = 0.001032 s +Y Equations = 0.00256437 s +E Equations = 0.000598 s +p Equations = 0.00221 s +calculate parcels = 155.509 s +chemistry correctThermo = 0.002892 s +turbulence correct = 0.001007 s +combustion correct(in Y) = 0.0994856 s +percentage of chemistry = 90.3183 % +percentage of rho/U/Y/E = 3.9504 % +========Time details of each equation======= +rhoEqn Time = 0.000303 s +rhoEqn assamble = 0.000237 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00103 s +UEqn assamble = 0.000608 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000422 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001813 s +YEqn assamble = 0.000649 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000144 s +YEqn correct boundary = 0 s +EEqn Time = 0.000442 s +EEqn assamble = 0.000331 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 224.41 s ClockTime = 225 s +Courant Number mean: 0.00488878 max: 0.0164193 +Time = 0.0017825 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21957 + Current mass in system = 1.34052e-09 + Linear momentum = (1.93556e-11 -7.06812e-09 0) + |Linear momentum| = 7.06815e-09 + Linear kinetic energy = 1.9954e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 423.004, 540.2 + Mass transfer phase change = 3.65618e-10 + D10, D32, Dmax (mu) = 61.3157, 84.9632, 177.854 + Liquid penetration 95% mass (m) = 0.0123052 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0142245, Final residual = 7.06677e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0294498, Final residual = 1.001e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000804482, Final residual = 5.37341e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000470596, Final residual = 3.89099e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000531596, Final residual = 4.66593e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000531569, Final residual = 4.67933e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000825655, Final residual = 5.32907e-08, No Iterations 1 +min/max(T) = 806.662, 2745.62 +GAMG: Solving for p, Initial residual = 0.0542623, Final residual = 0.000401077, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.78244e-05, global = 1.67988e-05, cumulative = 0.00832678 +GAMG: Solving for p, Initial residual = 0.00038343, Final residual = 1.99784e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.68975e-05, global = 1.6897e-05, cumulative = 0.00834368 +smoothSolver: Solving for epsilon, Initial residual = 0.000730694, Final residual = 8.18008e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000787657, Final residual = 1.35841e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.077948 s +other Time = 0 s +rho Equations = 0.000167 s +U Equations = 0.001152 s +Y Equations = 0.00247995 s +E Equations = 0.000655 s +p Equations = 0.001876 s +calculate parcels = 155.812 s +chemistry correctThermo = 0.001972 s +turbulence correct = 0.000849 s +combustion correct(in Y) = 0.06861 s +percentage of chemistry = 88.0203 % +percentage of rho/U/Y/E = 5.71401 % +========Time details of each equation======= +rhoEqn Time = 0.000292 s +rhoEqn assamble = 0.000231 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00115 s +UEqn assamble = 0.000707 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000443 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001901 s +YEqn assamble = 0.00059 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000273 s +YEqn correct boundary = 0 s +EEqn Time = 0.000529 s +EEqn assamble = 0.000423 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000106 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 224.79 s ClockTime = 225 s +Courant Number mean: 0.00490468 max: 0.0159193 +Time = 0.001785 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21957 + Current mass in system = 1.33906e-09 + Linear momentum = (1.93816e-11 -7.05548e-09 0) + |Linear momentum| = 7.0555e-09 + Linear kinetic energy = 1.9904e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 423.28, 540.2 + Mass transfer phase change = 3.67087e-10 + D10, D32, Dmax (mu) = 61.2531, 84.9146, 177.672 + Liquid penetration 95% mass (m) = 0.0123167 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0148317, Final residual = 7.49593e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0311998, Final residual = 1.07675e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000801106, Final residual = 5.2439e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000464452, Final residual = 3.77433e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000523932, Final residual = 4.53325e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000523897, Final residual = 4.54601e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000817979, Final residual = 5.22555e-08, No Iterations 1 +min/max(T) = 806.715, 2745.27 +GAMG: Solving for p, Initial residual = 0.0524041, Final residual = 0.000356925, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.77651e-05, global = 1.68394e-05, cumulative = 0.00836052 +GAMG: Solving for p, Initial residual = 0.000342545, Final residual = 2.41522e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.69267e-05, global = 1.69261e-05, cumulative = 0.00837744 +smoothSolver: Solving for epsilon, Initial residual = 0.000727491, Final residual = 8.11143e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000782388, Final residual = 1.34469e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.111756 s +other Time = 0 s +rho Equations = 0.000181 s +U Equations = 0.001277 s +Y Equations = 0.0024613 s +E Equations = 0.000627 s +p Equations = 0.002413 s +calculate parcels = 156.152 s +chemistry correctThermo = 0.00286 s +turbulence correct = 0.001252 s +combustion correct(in Y) = 0.100474 s +percentage of chemistry = 89.9045 % +percentage of rho/U/Y/E = 4.06806 % +========Time details of each equation======= +rhoEqn Time = 0.000347 s +rhoEqn assamble = 0.000275 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001276 s +UEqn assamble = 0.000776 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.0005 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001802 s +YEqn assamble = 0.000646 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000174 s +YEqn correct boundary = 0 s +EEqn Time = 0.000472 s +EEqn assamble = 0.000352 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00012 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 225.25 s ClockTime = 226 s +Courant Number mean: 0.00491324 max: 0.0154288 +Time = 0.0017875 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21956 + Current mass in system = 1.33758e-09 + Linear momentum = (1.94124e-11 -7.04278e-09 0) + |Linear momentum| = 7.04281e-09 + Linear kinetic energy = 1.98539e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 423.559, 540.2 + Mass transfer phase change = 3.68564e-10 + D10, D32, Dmax (mu) = 61.2376, 84.8678, 177.49 + Liquid penetration 95% mass (m) = 0.0123279 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0158638, Final residual = 7.97528e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0327845, Final residual = 1.14996e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000802214, Final residual = 5.17231e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000458388, Final residual = 3.65948e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000515823, Final residual = 4.40919e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000515793, Final residual = 4.42181e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000812566, Final residual = 5.15819e-08, No Iterations 1 +min/max(T) = 806.779, 2744.91 +GAMG: Solving for p, Initial residual = 0.050742, Final residual = 0.000317951, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.77584e-05, global = 1.69297e-05, cumulative = 0.00839437 +GAMG: Solving for p, Initial residual = 0.000308495, Final residual = 2.14805e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.70221e-05, global = 1.70217e-05, cumulative = 0.00841139 +smoothSolver: Solving for epsilon, Initial residual = 0.000725432, Final residual = 8.05941e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000777724, Final residual = 1.33095e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.112864 s +other Time = 0 s +rho Equations = 0.000183 s +U Equations = 0.001284 s +Y Equations = 0.0024352 s +E Equations = 0.000497 s +p Equations = 0.001882 s +calculate parcels = 156.48 s +chemistry correctThermo = 0.002017 s +turbulence correct = 0.000814 s +combustion correct(in Y) = 0.10356 s +percentage of chemistry = 91.7563 % +percentage of rho/U/Y/E = 3.89779 % +========Time details of each equation======= +rhoEqn Time = 0.000303 s +rhoEqn assamble = 0.000235 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001284 s +UEqn assamble = 0.000784 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.0005 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001814 s +YEqn assamble = 0.000635 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000168 s +YEqn correct boundary = 0 s +EEqn Time = 0.000374 s +EEqn assamble = 0.00028 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 225.69 s ClockTime = 226 s +Courant Number mean: 0.00491396 max: 0.0149226 +Time = 0.00179 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21956 + Current mass in system = 1.3361e-09 + Linear momentum = (1.94456e-11 -7.03007e-09 0) + |Linear momentum| = 7.0301e-09 + Linear kinetic energy = 1.98038e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 423.842, 540.2 + Mass transfer phase change = 3.70041e-10 + D10, D32, Dmax (mu) = 61.1732, 84.8182, 177.308 + Liquid penetration 95% mass (m) = 0.0123406 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0176253, Final residual = 8.68138e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0341219, Final residual = 1.21729e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000797828, Final residual = 5.0819e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000451519, Final residual = 3.5425e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000507783, Final residual = 4.29425e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00050777, Final residual = 4.30679e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000807973, Final residual = 5.10185e-08, No Iterations 1 +min/max(T) = 806.852, 2744.55 +GAMG: Solving for p, Initial residual = 0.0494429, Final residual = 0.000305784, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.77377e-05, global = 1.69263e-05, cumulative = 0.00842832 +GAMG: Solving for p, Initial residual = 0.000299612, Final residual = 2.50298e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.70262e-05, global = 1.70256e-05, cumulative = 0.00844535 +smoothSolver: Solving for epsilon, Initial residual = 0.000722721, Final residual = 8.0053e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000774285, Final residual = 1.31884e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.086037 s +other Time = 0 s +rho Equations = 0.000157 s +U Equations = 0.00098 s +Y Equations = 0.00241381 s +E Equations = 0.00064 s +p Equations = 0.002323 s +calculate parcels = 156.822 s +chemistry correctThermo = 0.002862 s +turbulence correct = 0.001069 s +combustion correct(in Y) = 0.0754062 s +percentage of chemistry = 87.6439 % +percentage of rho/U/Y/E = 4.87094 % +========Time details of each equation======= +rhoEqn Time = 0.000307 s +rhoEqn assamble = 0.000243 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000978 s +UEqn assamble = 0.000562 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000416 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001867 s +YEqn assamble = 0.000663 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000233 s +YEqn correct boundary = 0 s +EEqn Time = 0.000467 s +EEqn assamble = 0.000349 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 226.12 s ClockTime = 227 s +Courant Number mean: 0.00490552 max: 0.0147825 +Time = 0.0017925 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21956 + Current mass in system = 1.33462e-09 + Linear momentum = (1.94779e-11 -7.01733e-09 0) + |Linear momentum| = 7.01735e-09 + Linear kinetic energy = 1.97535e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 424.128, 540.2 + Mass transfer phase change = 3.71522e-10 + D10, D32, Dmax (mu) = 61.1082, 84.7681, 177.126 + Liquid penetration 95% mass (m) = 0.0123526 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0191667, Final residual = 9.41299e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.035109, Final residual = 1.27099e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000794705, Final residual = 4.98991e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000444043, Final residual = 3.4341e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000498506, Final residual = 4.16415e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000498497, Final residual = 4.17616e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000801581, Final residual = 5.00487e-08, No Iterations 1 +min/max(T) = 806.901, 2744.18 +GAMG: Solving for p, Initial residual = 0.0482426, Final residual = 0.000300951, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.78164e-05, global = 1.69666e-05, cumulative = 0.00846231 +GAMG: Solving for p, Initial residual = 0.000296752, Final residual = 2.39828e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.7071e-05, global = 1.70705e-05, cumulative = 0.00847938 +smoothSolver: Solving for epsilon, Initial residual = 0.000720617, Final residual = 7.94224e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000771634, Final residual = 1.30638e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09848 s +other Time = 0 s +rho Equations = 0.00019 s +U Equations = 0.001292 s +Y Equations = 0.00245172 s +E Equations = 0.000615 s +p Equations = 0.002335 s +calculate parcels = 157.164 s +chemistry correctThermo = 0.002873 s +turbulence correct = 0.0011 s +combustion correct(in Y) = 0.0874073 s +percentage of chemistry = 88.7564 % +percentage of rho/U/Y/E = 4.61892 % +========Time details of each equation======= +rhoEqn Time = 0.000354 s +rhoEqn assamble = 0.000279 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001291 s +UEqn assamble = 0.000764 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000527 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001766 s +YEqn assamble = 0.000651 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000157 s +YEqn correct boundary = 0 s +EEqn Time = 0.000448 s +EEqn assamble = 0.000331 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 226.56 s ClockTime = 227 s +Courant Number mean: 0.00488794 max: 0.0147729 +Time = 0.001795 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21955 + Current mass in system = 1.33313e-09 + Linear momentum = (1.95051e-11 -7.00453e-09 0) + |Linear momentum| = 7.00456e-09 + Linear kinetic energy = 1.97032e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 424.418, 540.2 + Mass transfer phase change = 3.73014e-10 + D10, D32, Dmax (mu) = 61.095, 84.7207, 176.944 + Liquid penetration 95% mass (m) = 0.012365 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0203144, Final residual = 9.95314e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0356161, Final residual = 1.30628e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000797473, Final residual = 4.9746e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000436703, Final residual = 3.32207e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000488959, Final residual = 4.03239e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000488961, Final residual = 4.04406e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000797079, Final residual = 4.94144e-08, No Iterations 1 +min/max(T) = 806.875, 2743.8 +GAMG: Solving for p, Initial residual = 0.047279, Final residual = 0.000329199, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.79688e-05, global = 1.70799e-05, cumulative = 0.00849646 +GAMG: Solving for p, Initial residual = 0.000325247, Final residual = 3.18897e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.71957e-05, global = 1.71952e-05, cumulative = 0.00851366 +smoothSolver: Solving for epsilon, Initial residual = 0.000720492, Final residual = 7.91384e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000770581, Final residual = 1.2968e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.085735 s +other Time = 1e-06 s +rho Equations = 0.000171 s +U Equations = 0.001037 s +Y Equations = 0.00220551 s +E Equations = 0.0005 s +p Equations = 0.001877 s +calculate parcels = 157.519 s +chemistry correctThermo = 0.001977 s +turbulence correct = 0.000831 s +combustion correct(in Y) = 0.0769565 s +percentage of chemistry = 89.7609 % +percentage of rho/U/Y/E = 4.56466 % +========Time details of each equation======= +rhoEqn Time = 0.000293 s +rhoEqn assamble = 0.000233 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001036 s +UEqn assamble = 0.000595 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000441 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001586 s +YEqn assamble = 0.000559 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000124 s +YEqn correct boundary = 0 s +EEqn Time = 0.000377 s +EEqn assamble = 0.000282 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 227 s ClockTime = 228 s +Courant Number mean: 0.00486195 max: 0.0148 +Time = 0.0017975 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21954 + Current mass in system = 1.33164e-09 + Linear momentum = (1.95315e-11 -6.99174e-09 0) + |Linear momentum| = 6.99177e-09 + Linear kinetic energy = 1.96529e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 424.711, 540.2 + Mass transfer phase change = 3.74503e-10 + D10, D32, Dmax (mu) = 61.0964, 84.6707, 176.762 + Liquid penetration 95% mass (m) = 0.0123781 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0212071, Final residual = 1.04627e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0356254, Final residual = 1.32102e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000790618, Final residual = 4.8709e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000429042, Final residual = 3.20466e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000480947, Final residual = 3.91974e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000480939, Final residual = 3.93117e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000791965, Final residual = 4.87517e-08, No Iterations 1 +min/max(T) = 806.849, 2743.41 +GAMG: Solving for p, Initial residual = 0.0463846, Final residual = 0.000345032, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.80071e-05, global = 1.70424e-05, cumulative = 0.0085307 +GAMG: Solving for p, Initial residual = 0.000340665, Final residual = 2.84026e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.7169e-05, global = 1.71683e-05, cumulative = 0.00854787 +smoothSolver: Solving for epsilon, Initial residual = 0.000718791, Final residual = 7.8448e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000769585, Final residual = 1.28566e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09594 s +other Time = 0 s +rho Equations = 0.00017 s +U Equations = 0.001022 s +Y Equations = 0.00237262 s +E Equations = 0.000597 s +p Equations = 0.002257 s +calculate parcels = 157.783 s +chemistry correctThermo = 0.002854 s +turbulence correct = 0.001134 s +combustion correct(in Y) = 0.0853414 s +percentage of chemistry = 88.9529 % +percentage of rho/U/Y/E = 4.33773 % +========Time details of each equation======= +rhoEqn Time = 0.00032 s +rhoEqn assamble = 0.000244 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001022 s +UEqn assamble = 0.000609 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000413 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001813 s +YEqn assamble = 0.000634 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000215 s +YEqn correct boundary = 0 s +EEqn Time = 0.000439 s +EEqn assamble = 0.000328 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 227.36 s ClockTime = 228 s +Courant Number mean: 0.00482693 max: 0.0147966 +Time = 0.0018 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21953 + Current mass in system = 1.33014e-09 + Linear momentum = (1.95667e-11 -6.97893e-09 0) + |Linear momentum| = 6.97896e-09 + Linear kinetic energy = 1.96025e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 424.928, 540.2 + Mass transfer phase change = 3.75998e-10 + D10, D32, Dmax (mu) = 61.0933, 84.621, 176.582 + Liquid penetration 95% mass (m) = 0.0123906 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0205456, Final residual = 1.0089e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0351444, Final residual = 1.3125e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000789339, Final residual = 4.8502e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000421548, Final residual = 3.08483e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000472569, Final residual = 3.79656e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000472579, Final residual = 3.80758e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000785998, Final residual = 4.79776e-08, No Iterations 1 +min/max(T) = 806.82, 2743.01 +GAMG: Solving for p, Initial residual = 0.0447342, Final residual = 0.000341233, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.811e-05, global = 1.71019e-05, cumulative = 0.00856497 +GAMG: Solving for p, Initial residual = 0.000335632, Final residual = 2.06236e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.72304e-05, global = 1.72299e-05, cumulative = 0.0085822 +smoothSolver: Solving for epsilon, Initial residual = 0.000716471, Final residual = 7.76911e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000767837, Final residual = 1.27312e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.108734 s +other Time = 0 s +rho Equations = 0.00018 s +U Equations = 0.001278 s +Y Equations = 0.00248629 s +E Equations = 0.000483 s +p Equations = 0.001833 s +calculate parcels = 158.152 s +chemistry correctThermo = 0.002016 s +turbulence correct = 0.000809 s +combustion correct(in Y) = 0.0994657 s +percentage of chemistry = 91.4762 % +percentage of rho/U/Y/E = 4.07167 % +========Time details of each equation======= +rhoEqn Time = 0.000297 s +rhoEqn assamble = 0.000234 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001276 s +UEqn assamble = 0.000785 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000491 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001836 s +YEqn assamble = 0.000639 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000162 s +YEqn correct boundary = 0 s +EEqn Time = 0.000363 s +EEqn assamble = 0.000272 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 228.15 s ClockTime = 229 s +Courant Number mean: 0.00478313 max: 0.0147955 +Time = 0.0018025 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21953 + Current mass in system = 1.32865e-09 + Linear momentum = (1.96096e-11 -6.9661e-09 0) + |Linear momentum| = 6.96612e-09 + Linear kinetic energy = 1.95521e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 425.123, 540.2 + Mass transfer phase change = 3.77494e-10 + D10, D32, Dmax (mu) = 61.0253, 84.569, 176.401 + Liquid penetration 95% mass (m) = 0.012403 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.019146, Final residual = 9.37029e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0341819, Final residual = 1.28203e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000783708, Final residual = 4.72898e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000413976, Final residual = 2.964e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00046525, Final residual = 3.67452e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000465235, Final residual = 3.6853e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000779769, Final residual = 4.69426e-08, No Iterations 1 +min/max(T) = 806.792, 2742.61 +GAMG: Solving for p, Initial residual = 0.0423323, Final residual = 0.000336205, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.81602e-05, global = 1.71085e-05, cumulative = 0.00859931 +GAMG: Solving for p, Initial residual = 0.000324022, Final residual = 2.24263e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.72438e-05, global = 1.72433e-05, cumulative = 0.00861655 +smoothSolver: Solving for epsilon, Initial residual = 0.000713135, Final residual = 7.69285e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000765507, Final residual = 1.26023e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097278 s +other Time = 1e-06 s +rho Equations = 0.000179 s +U Equations = 0.00129 s +Y Equations = 0.00250544 s +E Equations = 0.000606 s +p Equations = 0.002197 s +calculate parcels = 158.535 s +chemistry correctThermo = 0.002935 s +turbulence correct = 0.001033 s +combustion correct(in Y) = 0.0863306 s +percentage of chemistry = 88.7462 % +percentage of rho/U/Y/E = 4.7086 % +========Time details of each equation======= +rhoEqn Time = 0.000323 s +rhoEqn assamble = 0.000258 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001289 s +UEqn assamble = 0.000787 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000502 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001863 s +YEqn assamble = 0.000623 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000214 s +YEqn correct boundary = 0 s +EEqn Time = 0.000453 s +EEqn assamble = 0.000339 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 228.63 s ClockTime = 229 s +Courant Number mean: 0.00473051 max: 0.0147968 +Time = 0.001805 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21953 + Current mass in system = 1.32715e-09 + Linear momentum = (1.96559e-11 -6.95323e-09 0) + |Linear momentum| = 6.95325e-09 + Linear kinetic energy = 1.95016e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 425.318, 540.2 + Mass transfer phase change = 3.78995e-10 + D10, D32, Dmax (mu) = 60.9568, 84.5164, 176.221 + Liquid penetration 95% mass (m) = 0.0124139 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0173194, Final residual = 8.42568e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0327912, Final residual = 1.23096e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0007809, Final residual = 4.67139e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000406698, Final residual = 2.84696e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000458071, Final residual = 3.55982e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000458051, Final residual = 3.57028e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000776707, Final residual = 4.63884e-08, No Iterations 1 +min/max(T) = 806.763, 2742.21 +GAMG: Solving for p, Initial residual = 0.0398636, Final residual = 0.000306689, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.81827e-05, global = 1.7151e-05, cumulative = 0.0086337 +GAMG: Solving for p, Initial residual = 0.000298048, Final residual = 2.43895e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.72921e-05, global = 1.72915e-05, cumulative = 0.008651 +smoothSolver: Solving for epsilon, Initial residual = 0.000711008, Final residual = 7.63046e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000763134, Final residual = 1.24757e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09739 s +other Time = 1e-06 s +rho Equations = 0.000178 s +U Equations = 0.001209 s +Y Equations = 0.00215048 s +E Equations = 0.000485 s +p Equations = 0.001891 s +calculate parcels = 158.9 s +chemistry correctThermo = 0.002062 s +turbulence correct = 0.000858 s +combustion correct(in Y) = 0.0883515 s +percentage of chemistry = 90.7193 % +percentage of rho/U/Y/E = 4.13028 % +========Time details of each equation======= +rhoEqn Time = 0.000296 s +rhoEqn assamble = 0.000234 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001208 s +UEqn assamble = 0.000697 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000511 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001529 s +YEqn assamble = 0.000565 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000118 s +YEqn correct boundary = 0 s +EEqn Time = 0.000367 s +EEqn assamble = 0.000275 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 229.09 s ClockTime = 230 s +Courant Number mean: 0.00466916 max: 0.0147905 +Time = 0.0018075 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21952 + Current mass in system = 1.32564e-09 + Linear momentum = (1.97081e-11 -6.94031e-09 0) + |Linear momentum| = 6.94034e-09 + Linear kinetic energy = 1.94509e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 425.512, 540.2 + Mass transfer phase change = 3.805e-10 + D10, D32, Dmax (mu) = 60.9477, 84.4639, 176.042 + Liquid penetration 95% mass (m) = 0.0124252 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0162387, Final residual = 7.84945e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.031054, Final residual = 1.16342e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000779548, Final residual = 4.60122e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000399059, Final residual = 2.73717e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000450314, Final residual = 3.44527e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000450288, Final residual = 3.45538e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000776491, Final residual = 4.57848e-08, No Iterations 1 +min/max(T) = 806.736, 2741.81 +GAMG: Solving for p, Initial residual = 0.0381957, Final residual = 0.000283456, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.82323e-05, global = 1.7215e-05, cumulative = 0.00866821 +GAMG: Solving for p, Initial residual = 0.000276787, Final residual = 1.67097e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.73559e-05, global = 1.73555e-05, cumulative = 0.00868557 +smoothSolver: Solving for epsilon, Initial residual = 0.000708563, Final residual = 7.56093e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000760095, Final residual = 1.23327e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.078072 s +other Time = 1e-06 s +rho Equations = 0.000185 s +U Equations = 0.001066 s +Y Equations = 0.00222109 s +E Equations = 0.000494 s +p Equations = 0.001908 s +calculate parcels = 159.232 s +chemistry correctThermo = 0.001961 s +turbulence correct = 0.001387 s +combustion correct(in Y) = 0.0686459 s +percentage of chemistry = 87.9264 % +percentage of rho/U/Y/E = 5.08004 % +========Time details of each equation======= +rhoEqn Time = 0.000304 s +rhoEqn assamble = 0.000243 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001066 s +UEqn assamble = 0.000637 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000429 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001615 s +YEqn assamble = 0.000563 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000118 s +YEqn correct boundary = 0 s +EEqn Time = 0.000369 s +EEqn assamble = 0.000278 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 229.5 s ClockTime = 230 s +Courant Number mean: 0.00459872 max: 0.0147825 +Time = 0.00181 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21952 + Current mass in system = 1.32413e-09 + Linear momentum = (1.97661e-11 -6.92734e-09 0) + |Linear momentum| = 6.92736e-09 + Linear kinetic energy = 1.94001e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 425.707, 540.2 + Mass transfer phase change = 3.82011e-10 + D10, D32, Dmax (mu) = 60.8776, 84.4096, 175.856 + Liquid penetration 95% mass (m) = 0.0124361 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0157923, Final residual = 7.57721e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0289882, Final residual = 1.08285e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000778396, Final residual = 4.55532e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00039125, Final residual = 2.62733e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000442459, Final residual = 3.32851e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000442429, Final residual = 3.33837e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000779159, Final residual = 4.54942e-08, No Iterations 1 +min/max(T) = 806.71, 2741.41 +GAMG: Solving for p, Initial residual = 0.0366435, Final residual = 0.000266138, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.82686e-05, global = 1.72672e-05, cumulative = 0.00870283 +GAMG: Solving for p, Initial residual = 0.000260807, Final residual = 1.55885e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.74076e-05, global = 1.74072e-05, cumulative = 0.00872024 +smoothSolver: Solving for epsilon, Initial residual = 0.00070533, Final residual = 7.48874e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000755791, Final residual = 1.21765e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.104703 s +other Time = 0 s +rho Equations = 0.000181 s +U Equations = 0.001267 s +Y Equations = 0.00261322 s +E Equations = 0.000603 s +p Equations = 0.002194 s +calculate parcels = 159.511 s +chemistry correctThermo = 0.002903 s +turbulence correct = 0.000964 s +combustion correct(in Y) = 0.0937788 s +percentage of chemistry = 89.5665 % +percentage of rho/U/Y/E = 4.45472 % +========Time details of each equation======= +rhoEqn Time = 0.000322 s +rhoEqn assamble = 0.000256 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001267 s +UEqn assamble = 0.000771 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000496 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001949 s +YEqn assamble = 0.0007 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000192 s +YEqn correct boundary = 0 s +EEqn Time = 0.00044 s +EEqn assamble = 0.000327 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 229.89 s ClockTime = 230 s +Courant Number mean: 0.00451917 max: 0.0147725 +Time = 0.0018125 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21952 + Current mass in system = 1.32262e-09 + Linear momentum = (1.98324e-11 -6.91429e-09 0) + |Linear momentum| = 6.91432e-09 + Linear kinetic energy = 1.9349e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 425.902, 540.2 + Mass transfer phase change = 3.83527e-10 + D10, D32, Dmax (mu) = 60.8063, 84.3543, 176.202 + Liquid penetration 95% mass (m) = 0.0124466 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0160982, Final residual = 7.71565e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0291056, Final residual = 1.07173e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000777344, Final residual = 4.51009e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000383058, Final residual = 2.51703e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000434024, Final residual = 3.21276e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000434002, Final residual = 3.22226e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000781077, Final residual = 4.5154e-08, No Iterations 1 +min/max(T) = 806.686, 2741 +GAMG: Solving for p, Initial residual = 0.0352032, Final residual = 0.000247474, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.8329e-05, global = 1.73394e-05, cumulative = 0.00873758 +GAMG: Solving for p, Initial residual = 0.000242733, Final residual = 1.6118e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.74802e-05, global = 1.74796e-05, cumulative = 0.00875506 +smoothSolver: Solving for epsilon, Initial residual = 0.000701957, Final residual = 7.42188e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000751583, Final residual = 1.20159e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.10267 s +other Time = 0 s +rho Equations = 0.00019 s +U Equations = 0.001227 s +Y Equations = 0.00249011 s +E Equations = 0.000605 s +p Equations = 0.002481 s +calculate parcels = 159.869 s +chemistry correctThermo = 0.002902 s +turbulence correct = 0.001092 s +combustion correct(in Y) = 0.0914539 s +percentage of chemistry = 89.0756 % +percentage of rho/U/Y/E = 4.39476 % +========Time details of each equation======= +rhoEqn Time = 0.000352 s +rhoEqn assamble = 0.000277 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001227 s +UEqn assamble = 0.000729 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000498 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001859 s +YEqn assamble = 0.00069 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000191 s +YEqn correct boundary = 0 s +EEqn Time = 0.000445 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 230.35 s ClockTime = 231 s +Courant Number mean: 0.00443003 max: 0.0147619 +Time = 0.001815 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21951 + Current mass in system = 1.32109e-09 + Linear momentum = (1.99079e-11 -6.90115e-09 0) + |Linear momentum| = 6.90118e-09 + Linear kinetic energy = 1.92975e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 426.097, 540.2 + Mass transfer phase change = 3.85056e-10 + D10, D32, Dmax (mu) = 60.7775, 84.3002, 176.692 + Liquid penetration 95% mass (m) = 0.0124579 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0170963, Final residual = 8.10358e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.032462, Final residual = 1.16582e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000780372, Final residual = 4.53939e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000374482, Final residual = 2.41036e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000425824, Final residual = 3.09921e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00042581, Final residual = 3.10838e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000782886, Final residual = 4.4788e-08, No Iterations 1 +min/max(T) = 806.662, 2740.6 +GAMG: Solving for p, Initial residual = 0.0338027, Final residual = 0.000236428, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.84367e-05, global = 1.74847e-05, cumulative = 0.00877254 +GAMG: Solving for p, Initial residual = 0.000232084, Final residual = 1.76392e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.76193e-05, global = 1.76188e-05, cumulative = 0.00879016 +smoothSolver: Solving for epsilon, Initial residual = 0.000700277, Final residual = 7.3803e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000747793, Final residual = 1.18679e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094448 s +other Time = 0 s +rho Equations = 0.000163 s +U Equations = 0.001005 s +Y Equations = 0.00212713 s +E Equations = 0.000486 s +p Equations = 0.00236 s +calculate parcels = 160.203 s +chemistry correctThermo = 0.002005 s +turbulence correct = 0.001117 s +combustion correct(in Y) = 0.0850059 s +percentage of chemistry = 90.0028 % +percentage of rho/U/Y/E = 4.0034 % +========Time details of each equation======= +rhoEqn Time = 0.000315 s +rhoEqn assamble = 0.00025 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001002 s +UEqn assamble = 0.000587 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000415 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001553 s +YEqn assamble = 0.000523 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000167 s +YEqn correct boundary = 0 s +EEqn Time = 0.000366 s +EEqn assamble = 0.000273 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 230.78 s ClockTime = 231 s +Courant Number mean: 0.0043316 max: 0.0147862 +Time = 0.0018175 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21949 + Current mass in system = 1.31953e-09 + Linear momentum = (1.99914e-11 -6.8879e-09 0) + |Linear momentum| = 6.88793e-09 + Linear kinetic energy = 1.92458e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 426.293, 540.2 + Mass transfer phase change = 3.86611e-10 + D10, D32, Dmax (mu) = 60.8043, 84.2493, 177.184 + Liquid penetration 95% mass (m) = 0.0124695 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0189031, Final residual = 8.95152e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.036302, Final residual = 1.2762e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000784326, Final residual = 4.41706e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000365442, Final residual = 2.30286e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000415719, Final residual = 2.97096e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000415699, Final residual = 2.97993e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00078298, Final residual = 4.4328e-08, No Iterations 1 +min/max(T) = 806.64, 2740.2 +GAMG: Solving for p, Initial residual = 0.0326025, Final residual = 0.000270455, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.87802e-05, global = 1.77755e-05, cumulative = 0.00880794 +GAMG: Solving for p, Initial residual = 0.000263355, Final residual = 5.77296e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.79274e-05, global = 1.7926e-05, cumulative = 0.00882586 +smoothSolver: Solving for epsilon, Initial residual = 0.000694412, Final residual = 7.2983e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000741687, Final residual = 1.16747e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.110818 s +other Time = 0 s +rho Equations = 0.00018 s +U Equations = 0.001184 s +Y Equations = 0.00262494 s +E Equations = 0.000609 s +p Equations = 0.002206 s +calculate parcels = 160.552 s +chemistry correctThermo = 0.00287 s +turbulence correct = 0.001016 s +combustion correct(in Y) = 0.0999291 s +percentage of chemistry = 90.174 % +percentage of rho/U/Y/E = 4.14909 % +========Time details of each equation======= +rhoEqn Time = 0.000322 s +rhoEqn assamble = 0.000253 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001183 s +UEqn assamble = 0.000682 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000501 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001971 s +YEqn assamble = 0.000684 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000193 s +YEqn correct boundary = 0 s +EEqn Time = 0.000451 s +EEqn assamble = 0.00034 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 231.24 s ClockTime = 232 s +Courant Number mean: 0.00422458 max: 0.0148005 +Time = 0.00182 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21949 + Current mass in system = 1.31799e-09 + Linear momentum = (2.01008e-11 -6.87459e-09 0) + |Linear momentum| = 6.87462e-09 + Linear kinetic energy = 1.91938e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 426.488, 540.2 + Mass transfer phase change = 3.88151e-10 + D10, D32, Dmax (mu) = 60.7281, 84.1901, 177.677 + Liquid penetration 95% mass (m) = 0.0124823 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0225556, Final residual = 1.06215e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0401061, Final residual = 1.38449e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000778729, Final residual = 4.40288e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000354656, Final residual = 2.19135e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000408971, Final residual = 2.87817e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000408954, Final residual = 2.88685e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000781954, Final residual = 4.3817e-08, No Iterations 1 +min/max(T) = 806.619, 2739.78 +GAMG: Solving for p, Initial residual = 0.0314464, Final residual = 0.000279346, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.86836e-05, global = 1.76428e-05, cumulative = 0.00884351 +GAMG: Solving for p, Initial residual = 0.000269884, Final residual = 6.11256e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.77453e-05, global = 1.77436e-05, cumulative = 0.00886125 +smoothSolver: Solving for epsilon, Initial residual = 0.000694137, Final residual = 7.2925e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000739275, Final residual = 1.15674e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103659 s +other Time = 0 s +rho Equations = 0.000205 s +U Equations = 0.001012 s +Y Equations = 0.00237157 s +E Equations = 0.000594 s +p Equations = 0.00191 s +calculate parcels = 160.891 s +chemistry correctThermo = 0.00283 s +turbulence correct = 0.000856 s +combustion correct(in Y) = 0.0936704 s +percentage of chemistry = 90.364 % +percentage of rho/U/Y/E = 4.03493 % +========Time details of each equation======= +rhoEqn Time = 0.00033 s +rhoEqn assamble = 0.000259 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00101 s +UEqn assamble = 0.00059 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00042 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001822 s +YEqn assamble = 0.000633 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000227 s +YEqn correct boundary = 0 s +EEqn Time = 0.000441 s +EEqn assamble = 0.000327 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 231.68 s ClockTime = 232 s +Courant Number mean: 0.00410683 max: 0.0148031 +Time = 0.0018225 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21948 + Current mass in system = 1.31644e-09 + Linear momentum = (2.02185e-11 -6.86119e-09 0) + |Linear momentum| = 6.86122e-09 + Linear kinetic energy = 1.91414e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 426.683, 540.2 + Mass transfer phase change = 3.89701e-10 + D10, D32, Dmax (mu) = 60.7034, 84.1318, 178.167 + Liquid penetration 95% mass (m) = 0.0124944 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0239142, Final residual = 1.09092e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0436109, Final residual = 1.47504e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000776246, Final residual = 4.35552e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000345705, Final residual = 2.09284e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000400453, Final residual = 2.76906e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000400422, Final residual = 2.77742e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000775624, Final residual = 4.29569e-08, No Iterations 1 +min/max(T) = 806.599, 2739.36 +GAMG: Solving for p, Initial residual = 0.0297912, Final residual = 0.000211284, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.8694e-05, global = 1.77857e-05, cumulative = 0.00887904 +GAMG: Solving for p, Initial residual = 0.000204966, Final residual = 2.41666e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.78666e-05, global = 1.78655e-05, cumulative = 0.0088969 +smoothSolver: Solving for epsilon, Initial residual = 0.000689744, Final residual = 7.19592e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000734735, Final residual = 1.13701e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.077079 s +other Time = 1e-06 s +rho Equations = 0.000201 s +U Equations = 0.001048 s +Y Equations = 0.00213141 s +E Equations = 0.000476 s +p Equations = 0.001885 s +calculate parcels = 161.182 s +chemistry correctThermo = 0.002103 s +turbulence correct = 0.000816 s +combustion correct(in Y) = 0.0681616 s +percentage of chemistry = 88.4308 % +percentage of rho/U/Y/E = 5.00319 % +========Time details of each equation======= +rhoEqn Time = 0.000324 s +rhoEqn assamble = 0.000256 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001048 s +UEqn assamble = 0.000627 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000421 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001574 s +YEqn assamble = 0.000536 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000143 s +YEqn correct boundary = 0 s +EEqn Time = 0.000358 s +EEqn assamble = 0.000268 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 232.05 s ClockTime = 233 s +Courant Number mean: 0.00398035 max: 0.0147797 +Time = 0.001825 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21947 + Current mass in system = 1.31489e-09 + Linear momentum = (2.0333e-11 -6.84769e-09 0) + |Linear momentum| = 6.84772e-09 + Linear kinetic energy = 1.90887e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 426.879, 540.2 + Mass transfer phase change = 3.91257e-10 + D10, D32, Dmax (mu) = 60.6773, 84.072, 178.651 + Liquid penetration 95% mass (m) = 0.0125061 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0247576, Final residual = 1.09017e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0469166, Final residual = 1.55794e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000774706, Final residual = 4.31561e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000337667, Final residual = 2.01179e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000392985, Final residual = 2.67098e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000392952, Final residual = 2.67908e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000770364, Final residual = 4.21805e-08, No Iterations 1 +min/max(T) = 806.579, 2738.95 +GAMG: Solving for p, Initial residual = 0.0282005, Final residual = 0.000177951, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.86579e-05, global = 1.78741e-05, cumulative = 0.00891478 +GAMG: Solving for p, Initial residual = 0.00017254, Final residual = 2.54708e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.79433e-05, global = 1.79425e-05, cumulative = 0.00893272 +smoothSolver: Solving for epsilon, Initial residual = 0.000683856, Final residual = 7.11099e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00072982, Final residual = 1.11934e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.098426 s +other Time = 0 s +rho Equations = 0.000211 s +U Equations = 0.001226 s +Y Equations = 0.00249426 s +E Equations = 0.000599 s +p Equations = 0.002275 s +calculate parcels = 161.525 s +chemistry correctThermo = 0.002895 s +turbulence correct = 0.000996 s +combustion correct(in Y) = 0.0875227 s +percentage of chemistry = 88.9224 % +percentage of rho/U/Y/E = 4.60271 % +========Time details of each equation======= +rhoEqn Time = 0.000358 s +rhoEqn assamble = 0.000282 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001225 s +UEqn assamble = 0.000719 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000506 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001802 s +YEqn assamble = 0.000638 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000193 s +YEqn correct boundary = 0 s +EEqn Time = 0.000443 s +EEqn assamble = 0.000331 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 232.49 s ClockTime = 233 s +Courant Number mean: 0.00384703 max: 0.0147618 +Time = 0.0018275 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21947 + Current mass in system = 1.31332e-09 + Linear momentum = (2.04389e-11 -6.83409e-09 0) + |Linear momentum| = 6.83412e-09 + Linear kinetic energy = 1.90355e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 427.075, 540.2 + Mass transfer phase change = 3.92819e-10 + D10, D32, Dmax (mu) = 60.5971, 84.0092, 179.127 + Liquid penetration 95% mass (m) = 0.0125166 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0250937, Final residual = 1.0545e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0500429, Final residual = 1.62938e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000771298, Final residual = 4.24268e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000329811, Final residual = 1.94457e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000386012, Final residual = 2.58942e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000385973, Final residual = 2.5973e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000763553, Final residual = 4.12461e-08, No Iterations 1 +min/max(T) = 806.559, 2738.55 +GAMG: Solving for p, Initial residual = 0.0266632, Final residual = 0.000147836, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.86518e-05, global = 1.79478e-05, cumulative = 0.00895067 +GAMG: Solving for p, Initial residual = 0.000142952, Final residual = 1.4273e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.80028e-05, global = 1.80023e-05, cumulative = 0.00896867 +smoothSolver: Solving for epsilon, Initial residual = 0.000679281, Final residual = 7.05408e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000726591, Final residual = 1.10578e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.117164 s +other Time = 0 s +rho Equations = 0.000155 s +U Equations = 0.001004 s +Y Equations = 0.00232813 s +E Equations = 0.000485 s +p Equations = 0.001856 s +calculate parcels = 161.853 s +chemistry correctThermo = 0.002004 s +turbulence correct = 0.000944 s +combustion correct(in Y) = 0.108189 s +percentage of chemistry = 92.3397 % +percentage of rho/U/Y/E = 3.39023 % +========Time details of each equation======= +rhoEqn Time = 0.000275 s +rhoEqn assamble = 0.000219 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001003 s +UEqn assamble = 0.000577 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000426 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001763 s +YEqn assamble = 0.000623 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000183 s +YEqn correct boundary = 0 s +EEqn Time = 0.000364 s +EEqn assamble = 0.000272 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 232.93 s ClockTime = 233 s +Courant Number mean: 0.00370783 max: 0.0147507 +Time = 0.00183 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21946 + Current mass in system = 1.31175e-09 + Linear momentum = (2.05366e-11 -6.82031e-09 0) + |Linear momentum| = 6.82034e-09 + Linear kinetic energy = 1.89816e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 427.272, 540.2 + Mass transfer phase change = 3.94397e-10 + D10, D32, Dmax (mu) = 60.6191, 83.948, 179.592 + Liquid penetration 95% mass (m) = 0.0125282 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0248551, Final residual = 1.00551e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0529868, Final residual = 1.69269e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00077438, Final residual = 4.26697e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000322223, Final residual = 1.88048e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000378886, Final residual = 2.51138e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000378842, Final residual = 2.51919e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000756551, Final residual = 4.04117e-08, No Iterations 1 +min/max(T) = 806.539, 2738.16 +GAMG: Solving for p, Initial residual = 0.0251501, Final residual = 0.000143599, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.88015e-05, global = 1.81368e-05, cumulative = 0.00898681 +GAMG: Solving for p, Initial residual = 0.000137763, Final residual = 1.46751e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.81841e-05, global = 1.81837e-05, cumulative = 0.00900499 +smoothSolver: Solving for epsilon, Initial residual = 0.000676373, Final residual = 7.00703e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000725547, Final residual = 1.09556e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.112223 s +other Time = 1e-06 s +rho Equations = 0.000187 s +U Equations = 0.001268 s +Y Equations = 0.00253365 s +E Equations = 0.000654 s +p Equations = 0.0027 s +calculate parcels = 162.188 s +chemistry correctThermo = 0.002923 s +turbulence correct = 0.001196 s +combustion correct(in Y) = 0.100481 s +percentage of chemistry = 89.5372 % +percentage of rho/U/Y/E = 4.13698 % +========Time details of each equation======= +rhoEqn Time = 0.000369 s +rhoEqn assamble = 0.000289 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001268 s +UEqn assamble = 0.000765 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000503 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00188 s +YEqn assamble = 0.000687 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000202 s +YEqn correct boundary = 0 s +EEqn Time = 0.000477 s +EEqn assamble = 0.000358 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000119 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 233.38 s ClockTime = 234 s +Courant Number mean: 0.00356356 max: 0.014739 +Time = 0.0018325 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21946 + Current mass in system = 1.31016e-09 + Linear momentum = (2.06236e-11 -6.80635e-09 0) + |Linear momentum| = 6.80638e-09 + Linear kinetic energy = 1.8927e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 427.469, 540.2 + Mass transfer phase change = 3.9598e-10 + D10, D32, Dmax (mu) = 60.5352, 83.8815, 180.044 + Liquid penetration 95% mass (m) = 0.0125394 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0243542, Final residual = 9.68041e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0558002, Final residual = 1.74794e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000770056, Final residual = 4.15261e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000313982, Final residual = 1.81868e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000372342, Final residual = 2.43702e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000372293, Final residual = 2.4447e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000748439, Final residual = 3.94529e-08, No Iterations 1 +min/max(T) = 806.521, 2737.8 +GAMG: Solving for p, Initial residual = 0.0237416, Final residual = 0.000137229, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.89034e-05, global = 1.82089e-05, cumulative = 0.0090232 +GAMG: Solving for p, Initial residual = 0.000132059, Final residual = 8.33105e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.82545e-05, global = 1.82503e-05, cumulative = 0.00904145 +smoothSolver: Solving for epsilon, Initial residual = 0.000672546, Final residual = 6.96972e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00072455, Final residual = 1.08728e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.1044 s +other Time = 0 s +rho Equations = 0.000146 s +U Equations = 0.001104 s +Y Equations = 0.00203224 s +E Equations = 0.000496 s +p Equations = 0.001642 s +calculate parcels = 162.518 s +chemistry correctThermo = 0.002072 s +turbulence correct = 0.0008 s +combustion correct(in Y) = 0.0959358 s +percentage of chemistry = 91.8925 % +percentage of rho/U/Y/E = 3.619 % +========Time details of each equation======= +rhoEqn Time = 0.00026 s +rhoEqn assamble = 0.000208 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001102 s +UEqn assamble = 0.00067 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000432 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001472 s +YEqn assamble = 0.000511 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000143 s +YEqn correct boundary = 0 s +EEqn Time = 0.000375 s +EEqn assamble = 0.000281 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 233.82 s ClockTime = 234 s +Courant Number mean: 0.00341508 max: 0.0147182 +Time = 0.001835 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21946 + Current mass in system = 1.30857e-09 + Linear momentum = (2.06943e-11 -6.79216e-09 0) + |Linear momentum| = 6.79219e-09 + Linear kinetic energy = 1.88714e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 427.667, 540.2 + Mass transfer phase change = 3.97577e-10 + D10, D32, Dmax (mu) = 60.4496, 83.8128, 180.481 + Liquid penetration 95% mass (m) = 0.0125506 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.022586, Final residual = 8.88927e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0584738, Final residual = 1.7972e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000768948, Final residual = 4.0992e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000305469, Final residual = 1.7536e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000364788, Final residual = 2.36082e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00036474, Final residual = 2.36823e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000738862, Final residual = 3.84055e-08, No Iterations 1 +min/max(T) = 806.502, 2737.44 +GAMG: Solving for p, Initial residual = 0.022285, Final residual = 0.000131316, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.90479e-05, global = 1.83617e-05, cumulative = 0.00905981 +GAMG: Solving for p, Initial residual = 0.000126793, Final residual = 7.57564e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.84011e-05, global = 1.83979e-05, cumulative = 0.00907821 +smoothSolver: Solving for epsilon, Initial residual = 0.000667319, Final residual = 6.90951e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000722496, Final residual = 1.07591e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.079767 s +other Time = 0 s +rho Equations = 0.000216 s +U Equations = 0.001347 s +Y Equations = 0.00218415 s +E Equations = 0.000498 s +p Equations = 0.001768 s +calculate parcels = 162.896 s +chemistry correctThermo = 0.002059 s +turbulence correct = 0.000939 s +combustion correct(in Y) = 0.0705019 s +percentage of chemistry = 88.3847 % +percentage of rho/U/Y/E = 5.32194 % +========Time details of each equation======= +rhoEqn Time = 0.000341 s +rhoEqn assamble = 0.000269 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001346 s +UEqn assamble = 0.000827 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000519 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001499 s +YEqn assamble = 0.000524 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 7e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000375 s +EEqn assamble = 0.000282 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 234.27 s ClockTime = 235 s +Courant Number mean: 0.00326226 max: 0.0146914 +Time = 0.0018375 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21945 + Current mass in system = 1.30694e-09 + Linear momentum = (2.07422e-11 -6.77769e-09 0) + |Linear momentum| = 6.77773e-09 + Linear kinetic energy = 1.88148e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 427.865, 540.2 + Mass transfer phase change = 3.99206e-10 + D10, D32, Dmax (mu) = 60.3946, 83.7459, 180.639 + Liquid penetration 95% mass (m) = 0.0125618 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0206844, Final residual = 8.24884e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0610392, Final residual = 1.83983e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000776288, Final residual = 4.15714e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000296933, Final residual = 1.68927e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000354938, Final residual = 2.28791e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000354889, Final residual = 2.29536e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000729839, Final residual = 3.74473e-08, No Iterations 1 +min/max(T) = 806.485, 2737.1 +GAMG: Solving for p, Initial residual = 0.0209973, Final residual = 0.000156516, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.94537e-05, global = 1.87317e-05, cumulative = 0.00909694 +GAMG: Solving for p, Initial residual = 0.00015023, Final residual = 3.07577e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.87778e-05, global = 1.87766e-05, cumulative = 0.00911572 +smoothSolver: Solving for epsilon, Initial residual = 0.000658803, Final residual = 6.76215e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000718965, Final residual = 1.05947e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.096416 s +other Time = 0 s +rho Equations = 0.000242 s +U Equations = 0.001315 s +Y Equations = 0.00252452 s +E Equations = 0.000601 s +p Equations = 0.002229 s +calculate parcels = 163.155 s +chemistry correctThermo = 0.00289 s +turbulence correct = 0.001025 s +combustion correct(in Y) = 0.0853735 s +percentage of chemistry = 88.547 % +percentage of rho/U/Y/E = 4.85658 % +========Time details of each equation======= +rhoEqn Time = 0.000386 s +rhoEqn assamble = 0.000284 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000102 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001314 s +UEqn assamble = 0.000766 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000548 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001868 s +YEqn assamble = 0.000658 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000201 s +YEqn correct boundary = 0 s +EEqn Time = 0.000444 s +EEqn assamble = 0.000329 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 234.63 s ClockTime = 235 s +Courant Number mean: 0.00310646 max: 0.0148384 +Time = 0.00184 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21945 + Current mass in system = 1.30532e-09 + Linear momentum = (2.07556e-11 -6.76302e-09 0) + |Linear momentum| = 6.76305e-09 + Linear kinetic energy = 1.87572e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 428.063, 540.2 + Mass transfer phase change = 4.00828e-10 + D10, D32, Dmax (mu) = 60.3047, 83.6716, 180.452 + Liquid penetration 95% mass (m) = 0.0125736 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0220563, Final residual = 9.21362e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0635794, Final residual = 1.87785e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000771577, Final residual = 4.00628e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000287359, Final residual = 1.63135e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000349458, Final residual = 2.22149e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000349434, Final residual = 2.22871e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000721094, Final residual = 3.67908e-08, No Iterations 1 +min/max(T) = 806.468, 2736.75 +GAMG: Solving for p, Initial residual = 0.0198787, Final residual = 0.00016271, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.95393e-05, global = 1.86591e-05, cumulative = 0.00913437 +GAMG: Solving for p, Initial residual = 0.000155225, Final residual = 3.31922e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.86963e-05, global = 1.86948e-05, cumulative = 0.00915307 +smoothSolver: Solving for epsilon, Initial residual = 0.000659581, Final residual = 6.81809e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000719965, Final residual = 1.05712e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.105506 s +other Time = 0 s +rho Equations = 0.00018 s +U Equations = 0.001145 s +Y Equations = 0.00270377 s +E Equations = 0.000668 s +p Equations = 0.002639 s +calculate parcels = 163.515 s +chemistry correctThermo = 0.003235 s +turbulence correct = 0.001227 s +combustion correct(in Y) = 0.0935082 s +percentage of chemistry = 88.6284 % +percentage of rho/U/Y/E = 4.45166 % +========Time details of each equation======= +rhoEqn Time = 0.000365 s +rhoEqn assamble = 0.000288 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001144 s +UEqn assamble = 0.000696 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000448 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002046 s +YEqn assamble = 0.000726 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000237 s +YEqn correct boundary = 0 s +EEqn Time = 0.000495 s +EEqn assamble = 0.000375 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00012 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 235.09 s ClockTime = 236 s +Courant Number mean: 0.00294704 max: 0.0153194 +Time = 0.0018425 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21943 + Current mass in system = 1.30366e-09 + Linear momentum = (2.0738e-11 -6.74806e-09 0) + |Linear momentum| = 6.74809e-09 + Linear kinetic energy = 1.86986e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 428.262, 540.2 + Mass transfer phase change = 4.02483e-10 + D10, D32, Dmax (mu) = 60.2999, 83.6016, 180.266 + Liquid penetration 95% mass (m) = 0.0125858 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0216275, Final residual = 8.6401e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0659691, Final residual = 1.9081e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000773721, Final residual = 4.0369e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000279692, Final residual = 1.59252e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000341301, Final residual = 2.16232e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000341274, Final residual = 2.16945e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00070919, Final residual = 3.57157e-08, No Iterations 1 +min/max(T) = 806.454, 2736.42 +GAMG: Solving for p, Initial residual = 0.0185535, Final residual = 0.000151839, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.9809e-05, global = 1.90571e-05, cumulative = 0.00917213 +GAMG: Solving for p, Initial residual = 0.000145454, Final residual = 2.28654e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.90833e-05, global = 1.90824e-05, cumulative = 0.00919121 +smoothSolver: Solving for epsilon, Initial residual = 0.000652907, Final residual = 6.71019e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000718194, Final residual = 1.0457e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.105671 s +other Time = 0 s +rho Equations = 0.000181 s +U Equations = 0.001188 s +Y Equations = 0.00218732 s +E Equations = 0.000512 s +p Equations = 0.002334 s +calculate parcels = 163.864 s +chemistry correctThermo = 0.002274 s +turbulence correct = 0.00113 s +combustion correct(in Y) = 0.0956517 s +percentage of chemistry = 90.5184 % +percentage of rho/U/Y/E = 3.84999 % +========Time details of each equation======= +rhoEqn Time = 0.00033 s +rhoEqn assamble = 0.000259 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001188 s +UEqn assamble = 0.000685 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000503 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001539 s +YEqn assamble = 0.000544 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000137 s +YEqn correct boundary = 0 s +EEqn Time = 0.000393 s +EEqn assamble = 0.00028 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 235.55 s ClockTime = 236 s +Courant Number mean: 0.00278583 max: 0.0158348 +Time = 0.001845 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21940 + Current mass in system = 1.30198e-09 + Linear momentum = (2.06884e-11 -6.73284e-09 0) + |Linear momentum| = 6.73287e-09 + Linear kinetic energy = 1.8639e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 428.462, 540.2 + Mass transfer phase change = 4.04158e-10 + D10, D32, Dmax (mu) = 60.3385, 83.5304, 180.588 + Liquid penetration 95% mass (m) = 0.0125979 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0223043, Final residual = 8.9197e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0683535, Final residual = 1.93418e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000779076, Final residual = 4.00759e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000271722, Final residual = 1.56261e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000336461, Final residual = 2.11237e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000336457, Final residual = 2.11942e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000699465, Final residual = 3.49405e-08, No Iterations 1 +min/max(T) = 806.441, 2736.09 +GAMG: Solving for p, Initial residual = 0.0174508, Final residual = 0.000170533, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.01157e-05, global = 1.92752e-05, cumulative = 0.00921048 +GAMG: Solving for p, Initial residual = 0.000162723, Final residual = 5.41132e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.93093e-05, global = 1.93071e-05, cumulative = 0.00922979 +smoothSolver: Solving for epsilon, Initial residual = 0.000654551, Final residual = 6.72351e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000718918, Final residual = 1.04028e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.109842 s +other Time = 1e-06 s +rho Equations = 0.000205 s +U Equations = 0.001208 s +Y Equations = 0.0024901 s +E Equations = 0.000608 s +p Equations = 0.00227 s +calculate parcels = 164.229 s +chemistry correctThermo = 0.002877 s +turbulence correct = 0.000966 s +combustion correct(in Y) = 0.0990049 s +percentage of chemistry = 90.1339 % +percentage of rho/U/Y/E = 4.1069 % +========Time details of each equation======= +rhoEqn Time = 0.000375 s +rhoEqn assamble = 0.000299 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001207 s +UEqn assamble = 0.000702 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000505 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001852 s +YEqn assamble = 0.000662 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000197 s +YEqn correct boundary = 0 s +EEqn Time = 0.000446 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 236.03 s ClockTime = 237 s +Courant Number mean: 0.00262277 max: 0.0160484 +Time = 0.0018475 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21940 + Current mass in system = 1.30032e-09 + Linear momentum = (2.06446e-11 -6.71739e-09 0) + |Linear momentum| = 6.71742e-09 + Linear kinetic energy = 1.85782e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 428.661, 540.2 + Mass transfer phase change = 4.05821e-10 + D10, D32, Dmax (mu) = 60.2401, 83.4487, 181.022 + Liquid penetration 95% mass (m) = 0.0126095 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0248442, Final residual = 9.81849e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0708336, Final residual = 1.96016e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000768746, Final residual = 3.90037e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000264195, Final residual = 1.54243e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000335214, Final residual = 2.0929e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000335188, Final residual = 2.10007e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000688182, Final residual = 3.42334e-08, No Iterations 1 +min/max(T) = 806.43, 2735.78 +GAMG: Solving for p, Initial residual = 0.0162654, Final residual = 0.000171644, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.99867e-05, global = 1.91637e-05, cumulative = 0.00924896 +GAMG: Solving for p, Initial residual = 0.000163945, Final residual = 4.43623e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.91603e-05, global = 1.91584e-05, cumulative = 0.00926811 +smoothSolver: Solving for epsilon, Initial residual = 0.000652004, Final residual = 6.76426e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000719562, Final residual = 1.04174e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.110624 s +other Time = 0 s +rho Equations = 0.000203 s +U Equations = 0.001223 s +Y Equations = 0.00244108 s +E Equations = 0.000597 s +p Equations = 0.00233 s +calculate parcels = 164.526 s +chemistry correctThermo = 0.00293 s +turbulence correct = 0.001125 s +combustion correct(in Y) = 0.0995619 s +percentage of chemistry = 90.0003 % +percentage of rho/U/Y/E = 4.03536 % +========Time details of each equation======= +rhoEqn Time = 0.000349 s +rhoEqn assamble = 0.000262 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001223 s +UEqn assamble = 0.000691 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000532 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001788 s +YEqn assamble = 0.000635 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000181 s +YEqn correct boundary = 0 s +EEqn Time = 0.000439 s +EEqn assamble = 0.000326 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 236.43 s ClockTime = 237 s +Courant Number mean: 0.00245708 max: 0.0161253 +Time = 0.00185 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21939 + Current mass in system = 1.29864e-09 + Linear momentum = (2.06049e-11 -6.70164e-09 0) + |Linear momentum| = 6.70168e-09 + Linear kinetic energy = 1.85163e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 428.862, 540.2 + Mass transfer phase change = 4.07499e-10 + D10, D32, Dmax (mu) = 60.1882, 83.3659, 181.191 + Liquid penetration 95% mass (m) = 0.0126211 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0231991, Final residual = 8.49227e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0731591, Final residual = 1.98135e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000764976, Final residual = 3.84925e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000259178, Final residual = 1.52772e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000332486, Final residual = 2.06757e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000332453, Final residual = 2.07463e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000673699, Final residual = 3.32777e-08, No Iterations 1 +min/max(T) = 806.42, 2735.48 +GAMG: Solving for p, Initial residual = 0.0148762, Final residual = 0.000136674, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.0123e-05, global = 1.93408e-05, cumulative = 0.00928745 +GAMG: Solving for p, Initial residual = 0.00013071, Final residual = 1.97056e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.93414e-05, global = 1.93402e-05, cumulative = 0.00930679 +smoothSolver: Solving for epsilon, Initial residual = 0.000647381, Final residual = 6.69894e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000717741, Final residual = 1.03231e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.077909 s +other Time = 1e-06 s +rho Equations = 0.000168 s +U Equations = 0.001062 s +Y Equations = 0.00235079 s +E Equations = 0.000497 s +p Equations = 0.001928 s +calculate parcels = 164.834 s +chemistry correctThermo = 0.002008 s +turbulence correct = 0.001015 s +combustion correct(in Y) = 0.0686922 s +percentage of chemistry = 88.1698 % +percentage of rho/U/Y/E = 5.23404 % +========Time details of each equation======= +rhoEqn Time = 0.000293 s +rhoEqn assamble = 0.000234 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001059 s +UEqn assamble = 0.000634 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000425 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001776 s +YEqn assamble = 0.000574 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000158 s +YEqn correct boundary = 0 s +EEqn Time = 0.000367 s +EEqn assamble = 0.000276 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 236.82 s ClockTime = 237 s +Courant Number mean: 0.00229087 max: 0.0161947 +Time = 0.0018525 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21939 + Current mass in system = 1.29695e-09 + Linear momentum = (2.05585e-11 -6.68559e-09 0) + |Linear momentum| = 6.68562e-09 + Linear kinetic energy = 1.8453e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 429.063, 540.2 + Mass transfer phase change = 4.09189e-10 + D10, D32, Dmax (mu) = 60.0864, 83.2795, 181.001 + Liquid penetration 95% mass (m) = 0.0126326 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0208099, Final residual = 7.07084e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.075604, Final residual = 2.00157e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000761901, Final residual = 3.82362e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000254851, Final residual = 1.51774e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000331467, Final residual = 2.05543e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000331469, Final residual = 2.06257e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000660805, Final residual = 3.25629e-08, No Iterations 1 +min/max(T) = 806.411, 2735.19 +GAMG: Solving for p, Initial residual = 0.013599, Final residual = 0.000124743, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.02208e-05, global = 1.94729e-05, cumulative = 0.00932627 +GAMG: Solving for p, Initial residual = 0.000119402, Final residual = 1.52648e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.94833e-05, global = 1.94826e-05, cumulative = 0.00934575 +smoothSolver: Solving for epsilon, Initial residual = 0.000642542, Final residual = 6.63926e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000715899, Final residual = 1.02305e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.111167 s +other Time = 0 s +rho Equations = 0.000188 s +U Equations = 0.00124 s +Y Equations = 0.00243478 s +E Equations = 0.000601 s +p Equations = 0.002241 s +calculate parcels = 165.172 s +chemistry correctThermo = 0.002861 s +turbulence correct = 0.001032 s +combustion correct(in Y) = 0.100365 s +percentage of chemistry = 90.2833 % +percentage of rho/U/Y/E = 4.01539 % +========Time details of each equation======= +rhoEqn Time = 0.000343 s +rhoEqn assamble = 0.00027 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001238 s +UEqn assamble = 0.000727 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000511 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001802 s +YEqn assamble = 0.000651 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000195 s +YEqn correct boundary = 0 s +EEqn Time = 0.000447 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 237.27 s ClockTime = 238 s +Courant Number mean: 0.00212572 max: 0.0163102 +Time = 0.001855 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21939 + Current mass in system = 1.29525e-09 + Linear momentum = (2.05031e-11 -6.66918e-09 0) + |Linear momentum| = 6.66921e-09 + Linear kinetic energy = 1.83882e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 429.264, 540.2 + Mass transfer phase change = 4.10895e-10 + D10, D32, Dmax (mu) = 59.982, 83.1902, 180.81 + Liquid penetration 95% mass (m) = 0.0126435 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.017458, Final residual = 5.49026e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0781713, Final residual = 2.02001e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000761942, Final residual = 3.819e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000251526, Final residual = 1.52004e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000330927, Final residual = 2.04787e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000330956, Final residual = 2.055e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000649518, Final residual = 3.19504e-08, No Iterations 1 +min/max(T) = 806.404, 2734.92 +GAMG: Solving for p, Initial residual = 0.0124633, Final residual = 0.000112758, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.03657e-05, global = 1.96465e-05, cumulative = 0.0093654 +GAMG: Solving for p, Initial residual = 0.000108437, Final residual = 8.49702e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.96667e-05, global = 1.96628e-05, cumulative = 0.00938506 +smoothSolver: Solving for epsilon, Initial residual = 0.000639271, Final residual = 6.60891e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000714609, Final residual = 1.01583e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102385 s +other Time = 0 s +rho Equations = 0.000151 s +U Equations = 0.001112 s +Y Equations = 0.00212527 s +E Equations = 0.000476 s +p Equations = 0.001779 s +calculate parcels = 165.494 s +chemistry correctThermo = 0.002084 s +turbulence correct = 0.000909 s +combustion correct(in Y) = 0.0935737 s +percentage of chemistry = 91.394 % +percentage of rho/U/Y/E = 3.77426 % +========Time details of each equation======= +rhoEqn Time = 0.000274 s +rhoEqn assamble = 0.000217 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001111 s +UEqn assamble = 0.000583 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000528 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001419 s +YEqn assamble = 0.000517 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 6.3e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000359 s +EEqn assamble = 0.000268 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 237.69 s ClockTime = 238 s +Courant Number mean: 0.00196207 max: 0.0165563 +Time = 0.0018575 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21938 + Current mass in system = 1.29352e-09 + Linear momentum = (2.04442e-11 -6.65235e-09 0) + |Linear momentum| = 6.65238e-09 + Linear kinetic energy = 1.83217e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 429.466, 540.2 + Mass transfer phase change = 4.12623e-10 + D10, D32, Dmax (mu) = 59.9224, 83.0995, 180.619 + Liquid penetration 95% mass (m) = 0.0126538 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0145989, Final residual = 4.51906e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0808714, Final residual = 2.03844e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000764705, Final residual = 3.85365e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000248692, Final residual = 1.52948e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000330079, Final residual = 2.03685e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000330112, Final residual = 2.04395e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000638704, Final residual = 3.13477e-08, No Iterations 1 +min/max(T) = 806.397, 2734.67 +GAMG: Solving for p, Initial residual = 0.0113753, Final residual = 0.000104199, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.05711e-05, global = 1.98943e-05, cumulative = 0.00940495 +GAMG: Solving for p, Initial residual = 0.000100545, Final residual = 7.08112e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.99203e-05, global = 1.99163e-05, cumulative = 0.00942487 +smoothSolver: Solving for epsilon, Initial residual = 0.00063564, Final residual = 6.5972e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000713235, Final residual = 1.01007e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.111497 s +other Time = 0 s +rho Equations = 0.000155 s +U Equations = 0.001011 s +Y Equations = 0.00249157 s +E Equations = 0.000604 s +p Equations = 0.002076 s +calculate parcels = 165.837 s +chemistry correctThermo = 0.002863 s +turbulence correct = 0.001015 s +combustion correct(in Y) = 0.101096 s +percentage of chemistry = 90.6719 % +percentage of rho/U/Y/E = 3.82214 % +========Time details of each equation======= +rhoEqn Time = 0.000299 s +rhoEqn assamble = 0.000236 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00101 s +UEqn assamble = 0.000592 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000418 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001943 s +YEqn assamble = 0.000664 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000242 s +YEqn correct boundary = 0 s +EEqn Time = 0.000446 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 238.15 s ClockTime = 239 s +Courant Number mean: 0.00179998 max: 0.016825 +Time = 0.00186 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21935 + Current mass in system = 1.29177e-09 + Linear momentum = (2.0377e-11 -6.63504e-09 0) + |Linear momentum| = 6.63507e-09 + Linear kinetic energy = 1.82533e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 429.669, 540.2 + Mass transfer phase change = 4.14378e-10 + D10, D32, Dmax (mu) = 59.9258, 83.008, 180.426 + Liquid penetration 95% mass (m) = 0.0126642 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0128669, Final residual = 4.08499e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0837619, Final residual = 2.05782e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000769192, Final residual = 3.8619e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000245937, Final residual = 1.5369e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000328882, Final residual = 2.022e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000328905, Final residual = 2.02905e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000626744, Final residual = 3.06054e-08, No Iterations 1 +min/max(T) = 806.391, 2734.43 +GAMG: Solving for p, Initial residual = 0.0104797, Final residual = 0.000100723, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.08146e-05, global = 2.01938e-05, cumulative = 0.00944506 +GAMG: Solving for p, Initial residual = 9.74347e-05, Final residual = 8.22562e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.02279e-05, global = 2.02242e-05, cumulative = 0.00946529 +smoothSolver: Solving for epsilon, Initial residual = 0.000633531, Final residual = 6.59673e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000712268, Final residual = 1.00559e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.108876 s +other Time = 0 s +rho Equations = 0.000188 s +U Equations = 0.001288 s +Y Equations = 0.00256518 s +E Equations = 0.00063 s +p Equations = 0.002414 s +calculate parcels = 166.179 s +chemistry correctThermo = 0.002924 s +turbulence correct = 0.001082 s +combustion correct(in Y) = 0.0975678 s +percentage of chemistry = 89.6137 % +percentage of rho/U/Y/E = 4.29036 % +========Time details of each equation======= +rhoEqn Time = 0.000349 s +rhoEqn assamble = 0.000279 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001288 s +UEqn assamble = 0.000788 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.0005 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001907 s +YEqn assamble = 0.000651 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000183 s +YEqn correct boundary = 0 s +EEqn Time = 0.000467 s +EEqn assamble = 0.000349 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 238.6 s ClockTime = 239 s +Courant Number mean: 0.00164606 max: 0.01694 +Time = 0.0018625 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21935 + Current mass in system = 1.29e-09 + Linear momentum = (2.03075e-11 -6.61731e-09 0) + |Linear momentum| = 6.61734e-09 + Linear kinetic energy = 1.81831e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 429.872, 540.2 + Mass transfer phase change = 4.1614e-10 + D10, D32, Dmax (mu) = 59.8097, 82.9075, 180.232 + Liquid penetration 95% mass (m) = 0.0126751 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0134788, Final residual = 4.39709e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0867997, Final residual = 2.07714e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000761864, Final residual = 3.78378e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000242598, Final residual = 1.54093e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000328653, Final residual = 2.0251e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000328662, Final residual = 2.03212e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000613907, Final residual = 2.97618e-08, No Iterations 1 +min/max(T) = 806.387, 2734.2 +GAMG: Solving for p, Initial residual = 0.00997308, Final residual = 9.7922e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.09744e-05, global = 2.02856e-05, cumulative = 0.00948557 +GAMG: Solving for p, Initial residual = 9.51914e-05, Final residual = 2.08997e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.03185e-05, global = 2.0317e-05, cumulative = 0.00950589 +smoothSolver: Solving for epsilon, Initial residual = 0.000628267, Final residual = 6.58837e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000710042, Final residual = 1.00254e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.089406 s +other Time = 0 s +rho Equations = 0.000231 s +U Equations = 0.0013 s +Y Equations = 0.00263173 s +E Equations = 0.000688 s +p Equations = 0.002524 s +calculate parcels = 166.55 s +chemistry correctThermo = 0.003258 s +turbulence correct = 0.000918 s +combustion correct(in Y) = 0.0775663 s +percentage of chemistry = 86.7573 % +percentage of rho/U/Y/E = 5.42551 % +========Time details of each equation======= +rhoEqn Time = 0.000392 s +rhoEqn assamble = 0.000311 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001299 s +UEqn assamble = 0.000787 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000512 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001954 s +YEqn assamble = 0.000683 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000178 s +YEqn correct boundary = 0 s +EEqn Time = 0.000512 s +EEqn assamble = 0.000386 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000126 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 239.06 s ClockTime = 240 s +Courant Number mean: 0.00151283 max: 0.0169773 +Time = 0.001865 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21933 + Current mass in system = 1.28821e-09 + Linear momentum = (2.02296e-11 -6.59908e-09 0) + |Linear momentum| = 6.59911e-09 + Linear kinetic energy = 1.81109e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 430.076, 540.2 + Mass transfer phase change = 4.17929e-10 + D10, D32, Dmax (mu) = 59.7684, 82.8066, 180.608 + Liquid penetration 95% mass (m) = 0.0126855 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0129043, Final residual = 3.89067e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0900717, Final residual = 2.10722e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000763686, Final residual = 3.82001e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000239936, Final residual = 1.54604e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000326811, Final residual = 2.01361e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000326814, Final residual = 2.02071e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000605891, Final residual = 2.92718e-08, No Iterations 1 +min/max(T) = 806.384, 2733.98 +GAMG: Solving for p, Initial residual = 0.00957704, Final residual = 8.5281e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.11727e-05, global = 2.05872e-05, cumulative = 0.00952648 +GAMG: Solving for p, Initial residual = 8.32598e-05, Final residual = 8.10931e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.06187e-05, global = 2.06137e-05, cumulative = 0.00954709 +smoothSolver: Solving for epsilon, Initial residual = 0.000623039, Final residual = 6.55045e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000707504, Final residual = 9.96345e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100867 s +other Time = 0 s +rho Equations = 0.000169 s +U Equations = 0.001209 s +Y Equations = 0.00246612 s +E Equations = 0.000597 s +p Equations = 0.002038 s +calculate parcels = 166.811 s +chemistry correctThermo = 0.002873 s +turbulence correct = 0.001074 s +combustion correct(in Y) = 0.0902489 s +percentage of chemistry = 89.4731 % +percentage of rho/U/Y/E = 4.40295 % +========Time details of each equation======= +rhoEqn Time = 0.000313 s +rhoEqn assamble = 0.000248 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001207 s +UEqn assamble = 0.000764 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000443 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001703 s +YEqn assamble = 0.000629 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000115 s +YEqn correct boundary = 0 s +EEqn Time = 0.000441 s +EEqn assamble = 0.000327 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 239.42 s ClockTime = 240 s +Courant Number mean: 0.00139799 max: 0.0170007 +Time = 0.0018675 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21933 + Current mass in system = 1.28642e-09 + Linear momentum = (2.01382e-11 -6.58045e-09 0) + |Linear momentum| = 6.58048e-09 + Linear kinetic energy = 1.8037e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 430.281, 540.2 + Mass transfer phase change = 4.19728e-10 + D10, D32, Dmax (mu) = 59.6457, 82.6992, 181.088 + Liquid penetration 95% mass (m) = 0.0126968 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0134039, Final residual = 4.05377e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0935031, Final residual = 2.13975e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000757949, Final residual = 3.76021e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000237224, Final residual = 1.54688e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000326159, Final residual = 2.01624e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000326159, Final residual = 2.02369e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000599411, Final residual = 2.8897e-08, No Iterations 1 +min/max(T) = 806.383, 2733.78 +GAMG: Solving for p, Initial residual = 0.00936669, Final residual = 8.06507e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.12868e-05, global = 2.07053e-05, cumulative = 0.0095678 +GAMG: Solving for p, Initial residual = 7.90013e-05, Final residual = 7.27538e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.07375e-05, global = 2.07331e-05, cumulative = 0.00958853 +smoothSolver: Solving for epsilon, Initial residual = 0.000619641, Final residual = 6.54017e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000706256, Final residual = 9.93884e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.108282 s +other Time = 1e-06 s +rho Equations = 0.000153 s +U Equations = 0.001072 s +Y Equations = 0.00264784 s +E Equations = 0.000634 s +p Equations = 0.002161 s +calculate parcels = 167.17 s +chemistry correctThermo = 0.00292 s +turbulence correct = 0.000996 s +combustion correct(in Y) = 0.0975072 s +percentage of chemistry = 90.0493 % +percentage of rho/U/Y/E = 4.16213 % +========Time details of each equation======= +rhoEqn Time = 0.000314 s +rhoEqn assamble = 0.000248 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00107 s +UEqn assamble = 0.000662 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000408 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002093 s +YEqn assamble = 0.0007 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000263 s +YEqn correct boundary = 0 s +EEqn Time = 0.000463 s +EEqn assamble = 0.000341 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000122 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 239.89 s ClockTime = 240 s +Courant Number mean: 0.00130089 max: 0.0171969 +Time = 0.00187 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21933 + Current mass in system = 1.2846e-09 + Linear momentum = (2.00348e-11 -6.56145e-09 0) + |Linear momentum| = 6.56148e-09 + Linear kinetic energy = 1.79616e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 430.485, 540.2 + Mass transfer phase change = 4.21541e-10 + D10, D32, Dmax (mu) = 59.5209, 82.5892, 181.562 + Liquid penetration 95% mass (m) = 0.0127077 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0135831, Final residual = 3.99571e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0971934, Final residual = 2.18135e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000754937, Final residual = 3.75479e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000235261, Final residual = 1.55159e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000325015, Final residual = 2.01802e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000325009, Final residual = 2.02555e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00059316, Final residual = 2.86345e-08, No Iterations 1 +min/max(T) = 806.385, 2733.59 +GAMG: Solving for p, Initial residual = 0.00920128, Final residual = 7.50231e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.14414e-05, global = 2.0885e-05, cumulative = 0.00960941 +GAMG: Solving for p, Initial residual = 7.38521e-05, Final residual = 5.90904e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.0908e-05, global = 2.09042e-05, cumulative = 0.00963032 +smoothSolver: Solving for epsilon, Initial residual = 0.00061693, Final residual = 6.54039e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00070489, Final residual = 9.9181e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.093554 s +other Time = 1e-06 s +rho Equations = 0.000147 s +U Equations = 0.001029 s +Y Equations = 0.00210208 s +E Equations = 0.000495 s +p Equations = 0.001719 s +calculate parcels = 167.518 s +chemistry correctThermo = 0.002038 s +turbulence correct = 0.000805 s +combustion correct(in Y) = 0.0850469 s +percentage of chemistry = 90.9068 % +percentage of rho/U/Y/E = 4.03305 % +========Time details of each equation======= +rhoEqn Time = 0.000265 s +rhoEqn assamble = 0.000213 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001027 s +UEqn assamble = 0.000614 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000413 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001557 s +YEqn assamble = 0.000552 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000156 s +YEqn correct boundary = 0 s +EEqn Time = 0.000372 s +EEqn assamble = 0.000279 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 240.33 s ClockTime = 241 s +Courant Number mean: 0.0012219 max: 0.0173465 +Time = 0.0018725 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21933 + Current mass in system = 1.28277e-09 + Linear momentum = (1.99289e-11 -6.54215e-09 0) + |Linear momentum| = 6.54218e-09 + Linear kinetic energy = 1.78851e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 430.691, 540.2 + Mass transfer phase change = 4.23369e-10 + D10, D32, Dmax (mu) = 59.3939, 82.4766, 182.026 + Liquid penetration 95% mass (m) = 0.0127189 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0141591, Final residual = 4.18159e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.101096, Final residual = 2.23032e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000752875, Final residual = 3.74504e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000233237, Final residual = 1.55778e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00032381, Final residual = 2.02057e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000323822, Final residual = 2.02815e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000586896, Final residual = 2.82616e-08, No Iterations 1 +min/max(T) = 806.389, 2733.4 +GAMG: Solving for p, Initial residual = 0.00905182, Final residual = 7.43973e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.15962e-05, global = 2.10528e-05, cumulative = 0.00965137 +GAMG: Solving for p, Initial residual = 7.33471e-05, Final residual = 5.44618e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.10629e-05, global = 2.10591e-05, cumulative = 0.00967243 +smoothSolver: Solving for epsilon, Initial residual = 0.000613959, Final residual = 6.53514e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000703018, Final residual = 9.894e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.087895 s +other Time = 1e-06 s +rho Equations = 0.000158 s +U Equations = 0.000997 s +Y Equations = 0.00237271 s +E Equations = 0.000667 s +p Equations = 0.002183 s +calculate parcels = 167.885 s +chemistry correctThermo = 0.002828 s +turbulence correct = 0.001101 s +combustion correct(in Y) = 0.0774043 s +percentage of chemistry = 88.0645 % +percentage of rho/U/Y/E = 4.77241 % +========Time details of each equation======= +rhoEqn Time = 0.000304 s +rhoEqn assamble = 0.000241 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000996 s +UEqn assamble = 0.000578 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000418 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001854 s +YEqn assamble = 0.000628 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000243 s +YEqn correct boundary = 0 s +EEqn Time = 0.000452 s +EEqn assamble = 0.000339 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 240.79 s ClockTime = 241 s +Courant Number mean: 0.0011636 max: 0.0173395 +Time = 0.001875 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21931 + Current mass in system = 1.28093e-09 + Linear momentum = (1.98243e-11 -6.52251e-09 0) + |Linear momentum| = 6.52254e-09 + Linear kinetic energy = 1.78073e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 430.898, 540.2 + Mass transfer phase change = 4.25218e-10 + D10, D32, Dmax (mu) = 59.3442, 82.3654, 182.479 + Liquid penetration 95% mass (m) = 0.0127305 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0143609, Final residual = 4.24686e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.105121, Final residual = 2.28764e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000755239, Final residual = 3.78638e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000231564, Final residual = 1.5648e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000321932, Final residual = 2.01926e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000321936, Final residual = 2.02695e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000581638, Final residual = 2.79702e-08, No Iterations 1 +min/max(T) = 806.396, 2733.23 +GAMG: Solving for p, Initial residual = 0.00896582, Final residual = 7.75719e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.18378e-05, global = 2.13103e-05, cumulative = 0.00969374 +GAMG: Solving for p, Initial residual = 7.61799e-05, Final residual = 6.35704e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.13162e-05, global = 2.13122e-05, cumulative = 0.00971505 +smoothSolver: Solving for epsilon, Initial residual = 0.000610989, Final residual = 6.53296e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000700492, Final residual = 9.86858e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103091 s +other Time = 0 s +rho Equations = 0.000188 s +U Equations = 0.001206 s +Y Equations = 0.00357916 s +E Equations = 0.000962 s +p Equations = 0.001855 s +calculate parcels = 168.24 s +chemistry correctThermo = 0.004564 s +turbulence correct = 0.000921 s +combustion correct(in Y) = 0.0895948 s +percentage of chemistry = 86.9085 % +percentage of rho/U/Y/E = 5.75721 % +========Time details of each equation======= +rhoEqn Time = 0.000311 s +rhoEqn assamble = 0.000246 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001204 s +UEqn assamble = 0.0007 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000504 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002927 s +YEqn assamble = 0.000991 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00054 s +YEqn correct boundary = 0 s +EEqn Time = 0.000726 s +EEqn assamble = 0.000503 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000223 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 241.24 s ClockTime = 242 s +Courant Number mean: 0.00112893 max: 0.0172838 +Time = 0.0018775 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21929 + Current mass in system = 1.27906e-09 + Linear momentum = (1.97177e-11 -6.50255e-09 0) + |Linear momentum| = 6.50258e-09 + Linear kinetic energy = 1.77284e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 431.106, 540.2 + Mass transfer phase change = 4.27079e-10 + D10, D32, Dmax (mu) = 59.2987, 82.2511, 182.917 + Liquid penetration 95% mass (m) = 0.0127416 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0149324, Final residual = 4.5559e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.109152, Final residual = 2.3493e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000752587, Final residual = 3.68355e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00022981, Final residual = 1.57066e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000321148, Final residual = 2.02897e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000321137, Final residual = 2.03666e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00057674, Final residual = 2.77419e-08, No Iterations 1 +min/max(T) = 806.403, 2733.05 +GAMG: Solving for p, Initial residual = 0.00889493, Final residual = 7.76758e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.19858e-05, global = 2.14452e-05, cumulative = 0.0097365 +GAMG: Solving for p, Initial residual = 7.66519e-05, Final residual = 6.90567e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.14547e-05, global = 2.14504e-05, cumulative = 0.00975795 +smoothSolver: Solving for epsilon, Initial residual = 0.000606958, Final residual = 6.53471e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000698504, Final residual = 9.86822e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.077208 s +other Time = 0 s +rho Equations = 0.000172 s +U Equations = 0.001019 s +Y Equations = 0.00218869 s +E Equations = 0.000535 s +p Equations = 0.001776 s +calculate parcels = 168.557 s +chemistry correctThermo = 0.002013 s +turbulence correct = 0.000953 s +combustion correct(in Y) = 0.0683583 s +percentage of chemistry = 88.5379 % +percentage of rho/U/Y/E = 5.07032 % +========Time details of each equation======= +rhoEqn Time = 0.000301 s +rhoEqn assamble = 0.000239 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001018 s +UEqn assamble = 0.000604 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000414 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001626 s +YEqn assamble = 0.000566 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000156 s +YEqn correct boundary = 0 s +EEqn Time = 0.000386 s +EEqn assamble = 0.00029 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 241.64 s ClockTime = 242 s +Courant Number mean: 0.00111932 max: 0.0172751 +Time = 0.00188 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21927 + Current mass in system = 1.27717e-09 + Linear momentum = (1.95944e-11 -6.48224e-09 0) + |Linear momentum| = 6.48227e-09 + Linear kinetic energy = 1.76482e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 431.317, 540.2 + Mass transfer phase change = 4.28973e-10 + D10, D32, Dmax (mu) = 59.2378, 82.1377, 183.339 + Liquid penetration 95% mass (m) = 0.0127513 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0143912, Final residual = 4.26728e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.112759, Final residual = 2.41455e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000756584, Final residual = 3.79399e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000228539, Final residual = 1.57704e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000319264, Final residual = 2.02954e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000319246, Final residual = 2.03732e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000571916, Final residual = 2.74584e-08, No Iterations 1 +min/max(T) = 806.412, 2732.88 +GAMG: Solving for p, Initial residual = 0.00891563, Final residual = 8.84541e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.2361e-05, global = 2.18158e-05, cumulative = 0.00977976 +GAMG: Solving for p, Initial residual = 8.71631e-05, Final residual = 1.73597e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.18298e-05, global = 2.18287e-05, cumulative = 0.00980159 +smoothSolver: Solving for epsilon, Initial residual = 0.000605029, Final residual = 6.53472e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000695883, Final residual = 9.84553e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.115234 s +other Time = 1e-06 s +rho Equations = 0.000178 s +U Equations = 0.001254 s +Y Equations = 0.00245206 s +E Equations = 0.000641 s +p Equations = 0.002308 s +calculate parcels = 168.876 s +chemistry correctThermo = 0.002906 s +turbulence correct = 0.000991 s +combustion correct(in Y) = 0.104304 s +percentage of chemistry = 90.5149 % +percentage of rho/U/Y/E = 3.92684 % +========Time details of each equation======= +rhoEqn Time = 0.000329 s +rhoEqn assamble = 0.000261 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001252 s +UEqn assamble = 0.000742 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00051 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001784 s +YEqn assamble = 0.000644 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000168 s +YEqn correct boundary = 0 s +EEqn Time = 0.000479 s +EEqn assamble = 0.000364 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 242.07 s ClockTime = 243 s +Courant Number mean: 0.00113275 max: 0.0172361 +Time = 0.0018825 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21921 + Current mass in system = 1.27523e-09 + Linear momentum = (1.9461e-11 -6.46154e-09 0) + |Linear momentum| = 6.46157e-09 + Linear kinetic energy = 1.75667e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 431.528, 540.2 + Mass transfer phase change = 4.30909e-10 + D10, D32, Dmax (mu) = 59.3199, 82.0303, 183.611 + Liquid penetration 95% mass (m) = 0.012763 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0155441, Final residual = 5.25721e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.114624, Final residual = 2.45068e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000765028, Final residual = 3.8534e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000227051, Final residual = 1.58666e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000315529, Final residual = 2.02158e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000315509, Final residual = 2.02941e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000568636, Final residual = 2.74065e-08, No Iterations 1 +min/max(T) = 806.421, 2732.69 +GAMG: Solving for p, Initial residual = 0.00889168, Final residual = 0.000102968, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.29053e-05, global = 2.23078e-05, cumulative = 0.0098239 +GAMG: Solving for p, Initial residual = 0.000100956, Final residual = 2.55519e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.23168e-05, global = 2.23155e-05, cumulative = 0.00984622 +smoothSolver: Solving for epsilon, Initial residual = 0.000603242, Final residual = 6.52452e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000693606, Final residual = 9.83327e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.111309 s +other Time = 1e-06 s +rho Equations = 0.000182 s +U Equations = 0.001261 s +Y Equations = 0.00246194 s +E Equations = 0.000642 s +p Equations = 0.002229 s +calculate parcels = 169.234 s +chemistry correctThermo = 0.002854 s +turbulence correct = 0.000974 s +combustion correct(in Y) = 0.100494 s +percentage of chemistry = 90.2839 % +percentage of rho/U/Y/E = 4.08497 % +========Time details of each equation======= +rhoEqn Time = 0.000324 s +rhoEqn assamble = 0.000254 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001261 s +UEqn assamble = 0.000763 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000498 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001821 s +YEqn assamble = 0.000639 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000189 s +YEqn correct boundary = 0 s +EEqn Time = 0.000486 s +EEqn assamble = 0.000366 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00012 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 242.54 s ClockTime = 243 s +Courant Number mean: 0.00117102 max: 0.0171669 +Time = 0.001885 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21920 + Current mass in system = 1.27333e-09 + Linear momentum = (1.93283e-11 -6.44061e-09 0) + |Linear momentum| = 6.44064e-09 + Linear kinetic energy = 1.74842e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 431.741, 540.2 + Mass transfer phase change = 4.32811e-10 + D10, D32, Dmax (mu) = 59.207, 81.9069, 183.413 + Liquid penetration 95% mass (m) = 0.0127748 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0168203, Final residual = 5.85882e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.113655, Final residual = 2.44106e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000750225, Final residual = 3.69999e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000224711, Final residual = 1.59168e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000318408, Final residual = 2.05374e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000318356, Final residual = 2.06156e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000568063, Final residual = 2.74735e-08, No Iterations 1 +min/max(T) = 806.43, 2732.48 +GAMG: Solving for p, Initial residual = 0.00891071, Final residual = 0.000123545, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.27207e-05, global = 2.19366e-05, cumulative = 0.00986815 +GAMG: Solving for p, Initial residual = 0.000120028, Final residual = 2.10971e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.19226e-05, global = 2.19213e-05, cumulative = 0.00989007 +smoothSolver: Solving for epsilon, Initial residual = 0.000599461, Final residual = 6.63417e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000693568, Final residual = 9.99823e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.111999 s +other Time = 0 s +rho Equations = 0.000188 s +U Equations = 0.001266 s +Y Equations = 0.00241326 s +E Equations = 0.000614 s +p Equations = 0.001828 s +calculate parcels = 169.607 s +chemistry correctThermo = 0.00255 s +turbulence correct = 0.000812 s +combustion correct(in Y) = 0.102126 s +percentage of chemistry = 91.1845 % +percentage of rho/U/Y/E = 4.00116 % +========Time details of each equation======= +rhoEqn Time = 0.000304 s +rhoEqn assamble = 0.000241 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001265 s +UEqn assamble = 0.000766 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000499 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001754 s +YEqn assamble = 0.000638 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000168 s +YEqn correct boundary = 0 s +EEqn Time = 0.000457 s +EEqn assamble = 0.000333 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000124 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 243.03 s ClockTime = 244 s +Courant Number mean: 0.00123438 max: 0.0171484 +Time = 0.0018875 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21920 + Current mass in system = 1.27143e-09 + Linear momentum = (1.92028e-11 -6.41951e-09 0) + |Linear momentum| = 6.41954e-09 + Linear kinetic energy = 1.74011e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 431.956, 540.2 + Mass transfer phase change = 4.34716e-10 + D10, D32, Dmax (mu) = 59.0606, 81.7797, 183.214 + Liquid penetration 95% mass (m) = 0.0127859 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0155627, Final residual = 5.11369e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.110101, Final residual = 2.39981e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000743667, Final residual = 3.67051e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000223533, Final residual = 1.60434e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000318149, Final residual = 2.07079e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000318096, Final residual = 2.07859e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000560101, Final residual = 2.72075e-08, No Iterations 1 +min/max(T) = 806.44, 2732.27 +GAMG: Solving for p, Initial residual = 0.00902389, Final residual = 0.000106504, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.27313e-05, global = 2.19974e-05, cumulative = 0.00991207 +GAMG: Solving for p, Initial residual = 0.000104387, Final residual = 1.54959e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.19635e-05, global = 2.19625e-05, cumulative = 0.00993403 +smoothSolver: Solving for epsilon, Initial residual = 0.00059761, Final residual = 6.64451e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000690745, Final residual = 1.00244e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.096824 s +other Time = 0 s +rho Equations = 0.000154 s +U Equations = 0.001032 s +Y Equations = 0.00245119 s +E Equations = 0.000631 s +p Equations = 0.002282 s +calculate parcels = 169.965 s +chemistry correctThermo = 0.002884 s +turbulence correct = 0.000997 s +combustion correct(in Y) = 0.0861638 s +percentage of chemistry = 88.9901 % +percentage of rho/U/Y/E = 4.4082 % +========Time details of each equation======= +rhoEqn Time = 0.000304 s +rhoEqn assamble = 0.000238 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001032 s +UEqn assamble = 0.000621 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000411 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001907 s +YEqn assamble = 0.000638 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00024 s +YEqn correct boundary = 0 s +EEqn Time = 0.000474 s +EEqn assamble = 0.000357 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 243.48 s ClockTime = 244 s +Courant Number mean: 0.00132826 max: 0.017103 +Time = 0.00189 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21920 + Current mass in system = 1.26952e-09 + Linear momentum = (1.90897e-11 -6.39836e-09 0) + |Linear momentum| = 6.39839e-09 + Linear kinetic energy = 1.73179e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 432.172, 540.2 + Mass transfer phase change = 4.36628e-10 + D10, D32, Dmax (mu) = 58.9144, 81.6522, 183.015 + Liquid penetration 95% mass (m) = 0.0127959 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0129586, Final residual = 3.89024e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.104976, Final residual = 2.33711e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000740083, Final residual = 3.68061e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000223516, Final residual = 1.61743e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000317905, Final residual = 2.08319e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000317861, Final residual = 2.09108e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000555792, Final residual = 2.72239e-08, No Iterations 1 +min/max(T) = 806.449, 2732.1 +GAMG: Solving for p, Initial residual = 0.00914995, Final residual = 9.78442e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.27209e-05, global = 2.20734e-05, cumulative = 0.00995611 +GAMG: Solving for p, Initial residual = 9.50189e-05, Final residual = 1.71871e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.20287e-05, global = 2.20278e-05, cumulative = 0.00997814 +smoothSolver: Solving for epsilon, Initial residual = 0.000592721, Final residual = 6.60404e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000686015, Final residual = 1.00088e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.081073 s +other Time = 0 s +rho Equations = 0.000206 s +U Equations = 0.001362 s +Y Equations = 0.00239673 s +E Equations = 0.000532 s +p Equations = 0.001832 s +calculate parcels = 170.301 s +chemistry correctThermo = 0.001991 s +turbulence correct = 0.000892 s +combustion correct(in Y) = 0.0716453 s +percentage of chemistry = 88.3713 % +percentage of rho/U/Y/E = 5.54652 % +========Time details of each equation======= +rhoEqn Time = 0.000326 s +rhoEqn assamble = 0.000256 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001362 s +UEqn assamble = 0.000822 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00054 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001707 s +YEqn assamble = 0.000613 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.3e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000406 s +EEqn assamble = 0.00031 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 243.9 s ClockTime = 244 s +Courant Number mean: 0.00146809 max: 0.0169901 +Time = 0.0018925 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21920 + Current mass in system = 1.2676e-09 + Linear momentum = (1.89916e-11 -6.37719e-09 0) + |Linear momentum| = 6.37722e-09 + Linear kinetic energy = 1.72349e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 432.392, 540.2 + Mass transfer phase change = 4.38544e-10 + D10, D32, Dmax (mu) = 58.7689, 81.5243, 182.814 + Liquid penetration 95% mass (m) = 0.0128063 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0107549, Final residual = 3.14268e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.098278, Final residual = 2.24745e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000740079, Final residual = 3.70501e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000224263, Final residual = 1.63135e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000318842, Final residual = 2.09746e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000318796, Final residual = 2.10553e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000555686, Final residual = 2.75209e-08, No Iterations 1 +min/max(T) = 806.458, 2731.96 +GAMG: Solving for p, Initial residual = 0.00949933, Final residual = 9.54598e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.27496e-05, global = 2.21253e-05, cumulative = 0.0100003 +GAMG: Solving for p, Initial residual = 9.29434e-05, Final residual = 9.90465e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.20929e-05, global = 2.20877e-05, cumulative = 0.0100223 +smoothSolver: Solving for epsilon, Initial residual = 0.000589348, Final residual = 6.59874e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000681711, Final residual = 1.00222e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.116017 s +other Time = 1e-06 s +rho Equations = 0.000168 s +U Equations = 0.001606 s +Y Equations = 0.00254429 s +E Equations = 0.000482 s +p Equations = 0.001729 s +calculate parcels = 170.572 s +chemistry correctThermo = 0.002484 s +turbulence correct = 0.000839 s +combustion correct(in Y) = 0.105969 s +percentage of chemistry = 91.3389 % +percentage of rho/U/Y/E = 4.13758 % +========Time details of each equation======= +rhoEqn Time = 0.000288 s +rhoEqn assamble = 0.000228 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001605 s +UEqn assamble = 0.000707 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000898 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.000966 s +YEqn assamble = 0.000518 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -0.000373 s +YEqn correct boundary = 0 s +EEqn Time = 0.000364 s +EEqn assamble = 0.000271 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 244.29 s ClockTime = 245 s +Courant Number mean: 0.00161697 max: 0.016892 +Time = 0.001895 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21920 + Current mass in system = 1.26568e-09 + Linear momentum = (1.89112e-11 -6.35598e-09 0) + |Linear momentum| = 6.35601e-09 + Linear kinetic energy = 1.71519e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 432.615, 540.2 + Mass transfer phase change = 4.40466e-10 + D10, D32, Dmax (mu) = 58.6225, 81.3959, 182.612 + Liquid penetration 95% mass (m) = 0.012817 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0104991, Final residual = 3.43353e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0905849, Final residual = 2.13215e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00073915, Final residual = 3.73323e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000225349, Final residual = 1.64813e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00032003, Final residual = 2.11595e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000319982, Final residual = 2.12419e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000557448, Final residual = 2.77968e-08, No Iterations 1 +min/max(T) = 806.466, 2731.82 +GAMG: Solving for p, Initial residual = 0.0100133, Final residual = 9.28424e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.27972e-05, global = 2.21801e-05, cumulative = 0.0100445 +GAMG: Solving for p, Initial residual = 9.07347e-05, Final residual = 7.71863e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.21624e-05, global = 2.21579e-05, cumulative = 0.0100667 +smoothSolver: Solving for epsilon, Initial residual = 0.000587406, Final residual = 6.61852e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000678443, Final residual = 1.0064e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.113733 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001309 s +Y Equations = 0.00269009 s +E Equations = 0.000698 s +p Equations = 0.002608 s +calculate parcels = 170.918 s +chemistry correctThermo = 0.002949 s +turbulence correct = 0.001102 s +combustion correct(in Y) = 0.101972 s +percentage of chemistry = 89.659 % +percentage of rho/U/Y/E = 4.28555 % +========Time details of each equation======= +rhoEqn Time = 0.000369 s +rhoEqn assamble = 0.000291 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001309 s +UEqn assamble = 0.000801 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000508 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002049 s +YEqn assamble = 0.00073 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000221 s +YEqn correct boundary = 0 s +EEqn Time = 0.000525 s +EEqn assamble = 0.000401 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000124 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 244.75 s ClockTime = 245 s +Courant Number mean: 0.00176395 max: 0.0167911 +Time = 0.0018975 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21918 + Current mass in system = 1.26372e-09 + Linear momentum = (1.88548e-11 -6.33466e-09 0) + |Linear momentum| = 6.33469e-09 + Linear kinetic energy = 1.70688e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 432.841, 540.2 + Mass transfer phase change = 4.4242e-10 + D10, D32, Dmax (mu) = 58.5406, 81.2725, 182.409 + Liquid penetration 95% mass (m) = 0.0128279 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0123903, Final residual = 4.27756e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.082922, Final residual = 2.00973e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000744365, Final residual = 3.8474e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000227086, Final residual = 1.67143e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000320596, Final residual = 2.12574e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000320562, Final residual = 2.13423e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000562101, Final residual = 2.80465e-08, No Iterations 1 +min/max(T) = 806.475, 2731.67 +GAMG: Solving for p, Initial residual = 0.0107178, Final residual = 0.000116016, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.31383e-05, global = 2.25028e-05, cumulative = 0.0100892 +GAMG: Solving for p, Initial residual = 0.000113691, Final residual = 3.02873e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.25186e-05, global = 2.25173e-05, cumulative = 0.0101117 +smoothSolver: Solving for epsilon, Initial residual = 0.000587795, Final residual = 6.61762e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000675827, Final residual = 1.00898e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095816 s +other Time = 1e-06 s +rho Equations = 0.000186 s +U Equations = 0.001158 s +Y Equations = 0.00227778 s +E Equations = 0.000496 s +p Equations = 0.001814 s +calculate parcels = 171.286 s +chemistry correctThermo = 0.002038 s +turbulence correct = 0.000872 s +combustion correct(in Y) = 0.0867672 s +percentage of chemistry = 90.5561 % +percentage of rho/U/Y/E = 4.29759 % +========Time details of each equation======= +rhoEqn Time = 0.000304 s +rhoEqn assamble = 0.000239 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001157 s +UEqn assamble = 0.000658 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000499 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001577 s +YEqn assamble = 0.000562 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.4e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000372 s +EEqn assamble = 0.000278 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 245.21 s ClockTime = 246 s +Courant Number mean: 0.00190984 max: 0.0168489 +Time = 0.0019 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21917 + Current mass in system = 1.26178e-09 + Linear momentum = (1.88177e-11 -6.31325e-09 0) + |Linear momentum| = 6.31328e-09 + Linear kinetic energy = 1.69855e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 433.071, 540.2 + Mass transfer phase change = 4.44364e-10 + D10, D32, Dmax (mu) = 58.4177, 81.1436, 182.205 + Liquid penetration 95% mass (m) = 0.0128378 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0157764, Final residual = 5.84093e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0758066, Final residual = 1.89123e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000738376, Final residual = 3.74506e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000227376, Final residual = 1.68906e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000322362, Final residual = 2.14729e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000322318, Final residual = 2.1558e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000569361, Final residual = 2.82575e-08, No Iterations 1 +min/max(T) = 806.483, 2731.49 +GAMG: Solving for p, Initial residual = 0.0116398, Final residual = 0.000126667, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.31001e-05, global = 2.24048e-05, cumulative = 0.0101341 +GAMG: Solving for p, Initial residual = 0.000124156, Final residual = 3.10467e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.24065e-05, global = 2.24049e-05, cumulative = 0.0101565 +smoothSolver: Solving for epsilon, Initial residual = 0.000587798, Final residual = 6.73529e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000675416, Final residual = 1.02385e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.119298 s +other Time = 1e-06 s +rho Equations = 0.000158 s +U Equations = 0.001138 s +Y Equations = 0.00258643 s +E Equations = 0.0006 s +p Equations = 0.002184 s +calculate parcels = 171.588 s +chemistry correctThermo = 0.002859 s +turbulence correct = 0.000951 s +combustion correct(in Y) = 0.108653 s +percentage of chemistry = 91.0766 % +percentage of rho/U/Y/E = 3.75734 % +========Time details of each equation======= +rhoEqn Time = 0.000302 s +rhoEqn assamble = 0.000236 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001135 s +UEqn assamble = 0.000663 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000472 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00174 s +YEqn assamble = 0.000645 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.5e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000445 s +EEqn assamble = 0.000333 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 245.94 s ClockTime = 247 s +Courant Number mean: 0.00205234 max: 0.0169153 +Time = 0.0019025 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21917 + Current mass in system = 1.25983e-09 + Linear momentum = (1.88039e-11 -6.29175e-09 0) + |Linear momentum| = 6.29178e-09 + Linear kinetic energy = 1.69019e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 433.303, 540.2 + Mass transfer phase change = 4.4631e-10 + D10, D32, Dmax (mu) = 58.2667, 81.0117, 182.001 + Liquid penetration 95% mass (m) = 0.0128471 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0145171, Final residual = 4.60912e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0692085, Final residual = 1.77858e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000733002, Final residual = 3.74703e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000227222, Final residual = 1.70183e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000323058, Final residual = 2.16713e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000323005, Final residual = 2.17566e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000573863, Final residual = 2.8264e-08, No Iterations 1 +min/max(T) = 806.493, 2731.3 +GAMG: Solving for p, Initial residual = 0.012743, Final residual = 0.000116289, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.31656e-05, global = 2.24368e-05, cumulative = 0.010179 +GAMG: Solving for p, Initial residual = 0.00011501, Final residual = 2.63384e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.24326e-05, global = 2.24308e-05, cumulative = 0.0102014 +smoothSolver: Solving for epsilon, Initial residual = 0.000585324, Final residual = 6.74778e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000672839, Final residual = 1.02986e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.075176 s +other Time = 0 s +rho Equations = 0.000175 s +U Equations = 0.001135 s +Y Equations = 0.00225182 s +E Equations = 0.000488 s +p Equations = 0.001863 s +calculate parcels = 171.928 s +chemistry correctThermo = 0.001978 s +turbulence correct = 0.001027 s +combustion correct(in Y) = 0.0660652 s +percentage of chemistry = 87.8807 % +percentage of rho/U/Y/E = 5.38712 % +========Time details of each equation======= +rhoEqn Time = 0.000299 s +rhoEqn assamble = 0.000238 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001135 s +UEqn assamble = 0.000708 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000427 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001607 s +YEqn assamble = 0.000558 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.7e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000363 s +EEqn assamble = 0.000272 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 246.36 s ClockTime = 247 s +Courant Number mean: 0.00219015 max: 0.0169317 +Time = 0.001905 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21916 + Current mass in system = 1.25788e-09 + Linear momentum = (1.87882e-11 -6.27019e-09 0) + |Linear momentum| = 6.27022e-09 + Linear kinetic energy = 1.68183e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 433.538, 540.2 + Mass transfer phase change = 4.48266e-10 + D10, D32, Dmax (mu) = 58.1519, 80.881, 181.796 + Liquid penetration 95% mass (m) = 0.0128569 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0129009, Final residual = 4.19349e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0633465, Final residual = 1.67546e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000731389, Final residual = 3.74565e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000227596, Final residual = 1.71175e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000322544, Final residual = 2.17588e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000322493, Final residual = 2.18445e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000582197, Final residual = 2.8421e-08, No Iterations 1 +min/max(T) = 806.504, 2731.1 +GAMG: Solving for p, Initial residual = 0.0139296, Final residual = 0.000100969, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.3186e-05, global = 2.25459e-05, cumulative = 0.0102239 +GAMG: Solving for p, Initial residual = 9.97316e-05, Final residual = 1.89862e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.25452e-05, global = 2.25441e-05, cumulative = 0.0102465 +smoothSolver: Solving for epsilon, Initial residual = 0.000581711, Final residual = 6.72265e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000668969, Final residual = 1.03088e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.11277 s +other Time = 0 s +rho Equations = 0.000182 s +U Equations = 0.001263 s +Y Equations = 0.00240671 s +E Equations = 0.000625 s +p Equations = 0.002223 s +calculate parcels = 172.203 s +chemistry correctThermo = 0.002756 s +turbulence correct = 0.001026 s +combustion correct(in Y) = 0.10207 s +percentage of chemistry = 90.5119 % +percentage of rho/U/Y/E = 3.96977 % +========Time details of each equation======= +rhoEqn Time = 0.000329 s +rhoEqn assamble = 0.000259 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001263 s +UEqn assamble = 0.000769 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000494 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001772 s +YEqn assamble = 0.000634 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00018 s +YEqn correct boundary = 0 s +EEqn Time = 0.000452 s +EEqn assamble = 0.000337 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 246.75 s ClockTime = 247 s +Courant Number mean: 0.00232426 max: 0.0168612 +Time = 0.0019075 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21916 + Current mass in system = 1.25592e-09 + Linear momentum = (1.87524e-11 -6.24862e-09 0) + |Linear momentum| = 6.24865e-09 + Linear kinetic energy = 1.67349e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 433.776, 540.2 + Mass transfer phase change = 4.50224e-10 + D10, D32, Dmax (mu) = 58.0001, 80.7482, 181.59 + Liquid penetration 95% mass (m) = 0.0128674 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0121055, Final residual = 3.73825e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0580986, Final residual = 1.57637e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000727872, Final residual = 3.7376e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000228045, Final residual = 1.72257e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000323053, Final residual = 2.19433e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000322991, Final residual = 2.20297e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000592443, Final residual = 2.88018e-08, No Iterations 1 +min/max(T) = 806.515, 2730.91 +GAMG: Solving for p, Initial residual = 0.0152125, Final residual = 9.56407e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.31433e-05, global = 2.25656e-05, cumulative = 0.010269 +GAMG: Solving for p, Initial residual = 9.49079e-05, Final residual = 9.98686e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.25672e-05, global = 2.25622e-05, cumulative = 0.0102916 +smoothSolver: Solving for epsilon, Initial residual = 0.000579405, Final residual = 6.7177e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00066611, Final residual = 1.03393e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.089478 s +other Time = 0 s +rho Equations = 0.000184 s +U Equations = 0.001274 s +Y Equations = 0.00229125 s +E Equations = 0.000518 s +p Equations = 0.001642 s +calculate parcels = 172.533 s +chemistry correctThermo = 0.002026 s +turbulence correct = 0.000809 s +combustion correct(in Y) = 0.0805367 s +percentage of chemistry = 90.0073 % +percentage of rho/U/Y/E = 4.76905 % +========Time details of each equation======= +rhoEqn Time = 0.000302 s +rhoEqn assamble = 0.000238 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001271 s +UEqn assamble = 0.000757 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000514 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001632 s +YEqn assamble = 0.000558 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.1e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000397 s +EEqn assamble = 0.000301 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 247.17 s ClockTime = 248 s +Courant Number mean: 0.0024551 max: 0.016758 +Time = 0.00191 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21916 + Current mass in system = 1.25396e-09 + Linear momentum = (1.86878e-11 -6.22705e-09 0) + |Linear momentum| = 6.22708e-09 + Linear kinetic energy = 1.66517e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 434.017, 540.2 + Mass transfer phase change = 4.52186e-10 + D10, D32, Dmax (mu) = 57.8486, 80.6151, 181.385 + Liquid penetration 95% mass (m) = 0.0128791 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0110839, Final residual = 3.42875e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0534379, Final residual = 1.48581e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000727522, Final residual = 3.76393e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000228372, Final residual = 1.73573e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000323518, Final residual = 2.21298e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000323457, Final residual = 2.22167e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000601822, Final residual = 2.91638e-08, No Iterations 1 +min/max(T) = 806.525, 2730.74 +GAMG: Solving for p, Initial residual = 0.0166456, Final residual = 9.17579e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.31927e-05, global = 2.26231e-05, cumulative = 0.0103142 +GAMG: Solving for p, Initial residual = 9.16695e-05, Final residual = 6.94223e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.26224e-05, global = 2.26184e-05, cumulative = 0.0103368 +smoothSolver: Solving for epsilon, Initial residual = 0.000578356, Final residual = 6.73872e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000664042, Final residual = 1.03923e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.110479 s +other Time = 0 s +rho Equations = 0.00021 s +U Equations = 0.001133 s +Y Equations = 0.00249077 s +E Equations = 0.000607 s +p Equations = 0.002034 s +calculate parcels = 172.87 s +chemistry correctThermo = 0.002861 s +turbulence correct = 0.00096 s +combustion correct(in Y) = 0.0999672 s +percentage of chemistry = 90.4853 % +percentage of rho/U/Y/E = 4.01956 % +========Time details of each equation======= +rhoEqn Time = 0.000357 s +rhoEqn assamble = 0.00028 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001132 s +UEqn assamble = 0.000647 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000485 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001857 s +YEqn assamble = 0.00064 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000212 s +YEqn correct boundary = 0 s +EEqn Time = 0.000447 s +EEqn assamble = 0.000333 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 247.62 s ClockTime = 248 s +Courant Number mean: 0.00258258 max: 0.0169511 +Time = 0.0019125 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21915 + Current mass in system = 1.25198e-09 + Linear momentum = (1.85986e-11 -6.20547e-09 0) + |Linear momentum| = 6.20549e-09 + Linear kinetic energy = 1.65687e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 434.259, 540.2 + Mass transfer phase change = 4.5416e-10 + D10, D32, Dmax (mu) = 57.7267, 80.4842, 181.179 + Liquid penetration 95% mass (m) = 0.0128893 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00961944, Final residual = 3.04751e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0493615, Final residual = 1.40337e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000725204, Final residual = 3.73077e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000228712, Final residual = 1.74876e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000323039, Final residual = 2.22243e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000322982, Final residual = 2.23113e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000610733, Final residual = 2.94275e-08, No Iterations 1 +min/max(T) = 806.535, 2730.57 +GAMG: Solving for p, Initial residual = 0.018177, Final residual = 9.6462e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.33103e-05, global = 2.27545e-05, cumulative = 0.0103596 +GAMG: Solving for p, Initial residual = 9.66556e-05, Final residual = 9.13527e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.27592e-05, global = 2.27547e-05, cumulative = 0.0103824 +smoothSolver: Solving for epsilon, Initial residual = 0.000576729, Final residual = 6.75245e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000661885, Final residual = 1.04367e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103829 s +other Time = 1e-06 s +rho Equations = 0.000181 s +U Equations = 0.001162 s +Y Equations = 0.00221285 s +E Equations = 0.000496 s +p Equations = 0.002025 s +calculate parcels = 173.2 s +chemistry correctThermo = 0.002028 s +turbulence correct = 0.001036 s +combustion correct(in Y) = 0.0944942 s +percentage of chemistry = 91.0094 % +percentage of rho/U/Y/E = 3.90242 % +========Time details of each equation======= +rhoEqn Time = 0.000327 s +rhoEqn assamble = 0.000263 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001161 s +UEqn assamble = 0.000662 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000499 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00157 s +YEqn assamble = 0.000554 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000109 s +YEqn correct boundary = 0 s +EEqn Time = 0.000373 s +EEqn assamble = 0.000279 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 248.05 s ClockTime = 249 s +Courant Number mean: 0.00270658 max: 0.0171642 +Time = 0.001915 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21915 + Current mass in system = 1.25001e-09 + Linear momentum = (1.85055e-11 -6.1839e-09 0) + |Linear momentum| = 6.18393e-09 + Linear kinetic energy = 1.6486e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 434.504, 540.2 + Mass transfer phase change = 4.56132e-10 + D10, D32, Dmax (mu) = 57.5749, 80.3504, 181.291 + Liquid penetration 95% mass (m) = 0.0128999 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00859044, Final residual = 2.95919e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0457839, Final residual = 1.32808e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000724078, Final residual = 3.78915e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000228748, Final residual = 1.76243e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000323996, Final residual = 2.24588e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000323944, Final residual = 2.25468e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000618611, Final residual = 2.99287e-08, No Iterations 1 +min/max(T) = 806.543, 2730.41 +GAMG: Solving for p, Initial residual = 0.0198095, Final residual = 0.000106094, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.33158e-05, global = 2.27234e-05, cumulative = 0.0104051 +GAMG: Solving for p, Initial residual = 0.000106771, Final residual = 9.95166e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.27272e-05, global = 2.27225e-05, cumulative = 0.0104278 +smoothSolver: Solving for epsilon, Initial residual = 0.000576318, Final residual = 6.78773e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000661293, Final residual = 1.05135e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100942 s +other Time = 0 s +rho Equations = 0.000214 s +U Equations = 0.001015 s +Y Equations = 0.00269918 s +E Equations = 0.00067 s +p Equations = 0.001731 s +calculate parcels = 173.519 s +chemistry correctThermo = 0.003151 s +turbulence correct = 0.000853 s +combustion correct(in Y) = 0.0904238 s +percentage of chemistry = 89.58 % +percentage of rho/U/Y/E = 4.55527 % +========Time details of each equation======= +rhoEqn Time = 0.000339 s +rhoEqn assamble = 0.000222 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000117 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001014 s +UEqn assamble = 0.000601 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000413 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002156 s +YEqn assamble = 0.000723 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000281 s +YEqn correct boundary = 0 s +EEqn Time = 0.000502 s +EEqn assamble = 0.000368 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000134 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 248.47 s ClockTime = 249 s +Courant Number mean: 0.00282656 max: 0.0175941 +Time = 0.0019175 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21914 + Current mass in system = 1.24803e-09 + Linear momentum = (1.84246e-11 -6.16233e-09 0) + |Linear momentum| = 6.16235e-09 + Linear kinetic energy = 1.64035e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 434.751, 540.2 + Mass transfer phase change = 4.58111e-10 + D10, D32, Dmax (mu) = 57.4662, 80.2179, 181.469 + Liquid penetration 95% mass (m) = 0.0129094 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00849363, Final residual = 2.882e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0425839, Final residual = 1.25889e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000722592, Final residual = 3.80376e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000229322, Final residual = 1.77536e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000323762, Final residual = 2.25728e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000323701, Final residual = 2.2661e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000625403, Final residual = 3.02088e-08, No Iterations 1 +min/max(T) = 806.552, 2730.25 +GAMG: Solving for p, Initial residual = 0.0215612, Final residual = 0.00010127, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.33645e-05, global = 2.28137e-05, cumulative = 0.0104506 +GAMG: Solving for p, Initial residual = 0.000102531, Final residual = 6.28807e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.28176e-05, global = 2.28142e-05, cumulative = 0.0104734 +smoothSolver: Solving for epsilon, Initial residual = 0.000574522, Final residual = 6.80003e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000659603, Final residual = 1.05538e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.078354 s +other Time = 0 s +rho Equations = 0.000187 s +U Equations = 0.00114 s +Y Equations = 0.00222992 s +E Equations = 0.000536 s +p Equations = 0.001779 s +calculate parcels = 173.832 s +chemistry correctThermo = 0.001998 s +turbulence correct = 0.00084 s +combustion correct(in Y) = 0.0693601 s +percentage of chemistry = 88.5214 % +percentage of rho/U/Y/E = 5.22363 % +========Time details of each equation======= +rhoEqn Time = 0.000309 s +rhoEqn assamble = 0.000245 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001138 s +UEqn assamble = 0.000712 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000426 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001644 s +YEqn assamble = 0.00055 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000128 s +YEqn correct boundary = 0 s +EEqn Time = 0.000415 s +EEqn assamble = 0.000319 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 248.86 s ClockTime = 249 s +Courant Number mean: 0.00294274 max: 0.0177258 +Time = 0.00192 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21914 + Current mass in system = 1.24605e-09 + Linear momentum = (1.83398e-11 -6.14075e-09 0) + |Linear momentum| = 6.14078e-09 + Linear kinetic energy = 1.63211e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 435.001, 540.2 + Mass transfer phase change = 4.60091e-10 + D10, D32, Dmax (mu) = 57.3146, 80.083, 181.269 + Liquid penetration 95% mass (m) = 0.0129192 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00880852, Final residual = 3.0853e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0397099, Final residual = 1.19473e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000717585, Final residual = 3.79615e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000229735, Final residual = 1.78895e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000324422, Final residual = 2.27967e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000324372, Final residual = 2.28859e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000632073, Final residual = 3.05153e-08, No Iterations 1 +min/max(T) = 806.561, 2730.1 +GAMG: Solving for p, Initial residual = 0.0234069, Final residual = 0.000103591, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.33746e-05, global = 2.28101e-05, cumulative = 0.0104962 +GAMG: Solving for p, Initial residual = 0.000105508, Final residual = 6.50572e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.28282e-05, global = 2.28251e-05, cumulative = 0.0105191 +smoothSolver: Solving for epsilon, Initial residual = 0.00057431, Final residual = 6.81558e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000658782, Final residual = 1.05977e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.113555 s +other Time = 0 s +rho Equations = 0.000186 s +U Equations = 0.001289 s +Y Equations = 0.00248615 s +E Equations = 0.000605 s +p Equations = 0.002019 s +calculate parcels = 174.151 s +chemistry correctThermo = 0.002906 s +turbulence correct = 0.000957 s +combustion correct(in Y) = 0.102887 s +percentage of chemistry = 90.6053 % +percentage of rho/U/Y/E = 4.02109 % +========Time details of each equation======= +rhoEqn Time = 0.000328 s +rhoEqn assamble = 0.000255 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001289 s +UEqn assamble = 0.000787 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000502 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001839 s +YEqn assamble = 0.000659 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000184 s +YEqn correct boundary = 0 s +EEqn Time = 0.000451 s +EEqn assamble = 0.000338 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 249.29 s ClockTime = 250 s +Courant Number mean: 0.00305523 max: 0.0179339 +Time = 0.0019225 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21913 + Current mass in system = 1.24404e-09 + Linear momentum = (1.82597e-11 -6.11909e-09 0) + |Linear momentum| = 6.11911e-09 + Linear kinetic energy = 1.62388e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 435.253, 540.2 + Mass transfer phase change = 4.62101e-10 + D10, D32, Dmax (mu) = 57.1915, 79.9526, 181.068 + Liquid penetration 95% mass (m) = 0.0129276 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00953756, Final residual = 3.31869e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0371318, Final residual = 1.1353e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000722627, Final residual = 3.96083e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000230151, Final residual = 1.80606e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000324494, Final residual = 2.29956e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000324448, Final residual = 2.30874e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000638445, Final residual = 3.09714e-08, No Iterations 1 +min/max(T) = 806.57, 2729.96 +GAMG: Solving for p, Initial residual = 0.0254785, Final residual = 0.000132261, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.36553e-05, global = 2.31238e-05, cumulative = 0.0105422 +GAMG: Solving for p, Initial residual = 0.000134331, Final residual = 3.95992e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.31603e-05, global = 2.31592e-05, cumulative = 0.0105653 +smoothSolver: Solving for epsilon, Initial residual = 0.000573624, Final residual = 6.77559e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000657631, Final residual = 1.05838e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094386 s +other Time = 0 s +rho Equations = 0.000181 s +U Equations = 0.001198 s +Y Equations = 0.00226936 s +E Equations = 0.000497 s +p Equations = 0.002263 s +calculate parcels = 174.518 s +chemistry correctThermo = 0.002067 s +turbulence correct = 0.00103 s +combustion correct(in Y) = 0.0846856 s +percentage of chemistry = 89.7227 % +percentage of rho/U/Y/E = 4.39192 % +========Time details of each equation======= +rhoEqn Time = 0.000314 s +rhoEqn assamble = 0.000248 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001196 s +UEqn assamble = 0.000678 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000518 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001611 s +YEqn assamble = 0.000603 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000121 s +YEqn correct boundary = 0 s +EEqn Time = 0.000369 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 249.76 s ClockTime = 250 s +Courant Number mean: 0.00316518 max: 0.0180124 +Time = 0.001925 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21913 + Current mass in system = 1.24205e-09 + Linear momentum = (1.81861e-11 -6.09734e-09 0) + |Linear momentum| = 6.09737e-09 + Linear kinetic energy = 1.61563e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 435.507, 540.2 + Mass transfer phase change = 4.64095e-10 + D10, D32, Dmax (mu) = 57.0375, 79.8161, 180.869 + Liquid penetration 95% mass (m) = 0.0129377 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0116174, Final residual = 4.69282e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0349285, Final residual = 1.08583e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000716551, Final residual = 3.8176e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00022951, Final residual = 1.82057e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000324419, Final residual = 2.31748e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000324366, Final residual = 2.32661e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000646355, Final residual = 3.12339e-08, No Iterations 1 +min/max(T) = 806.58, 2729.81 +GAMG: Solving for p, Initial residual = 0.0276325, Final residual = 0.000171383, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.36159e-05, global = 2.29671e-05, cumulative = 0.0105883 +GAMG: Solving for p, Initial residual = 0.000173003, Final residual = 5.38882e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.29838e-05, global = 2.2982e-05, cumulative = 0.0106113 +smoothSolver: Solving for epsilon, Initial residual = 0.000572561, Final residual = 6.87281e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000658212, Final residual = 1.07273e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.105389 s +other Time = 0 s +rho Equations = 0.000178 s +U Equations = 0.001173 s +Y Equations = 0.0021538 s +E Equations = 0.000485 s +p Equations = 0.002035 s +calculate parcels = 174.898 s +chemistry correctThermo = 0.002032 s +turbulence correct = 0.000927 s +combustion correct(in Y) = 0.0962022 s +percentage of chemistry = 91.283 % +percentage of rho/U/Y/E = 3.78579 % +========Time details of each equation======= +rhoEqn Time = 0.000306 s +rhoEqn assamble = 0.00024 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001173 s +UEqn assamble = 0.000682 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000491 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001513 s +YEqn assamble = 0.000545 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000367 s +EEqn assamble = 0.000275 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 250.24 s ClockTime = 251 s +Courant Number mean: 0.00327095 max: 0.0183069 +Time = 0.0019275 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21912 + Current mass in system = 1.24003e-09 + Linear momentum = (1.81163e-11 -6.07536e-09 0) + |Linear momentum| = 6.07539e-09 + Linear kinetic energy = 1.60731e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 435.763, 540.2 + Mass transfer phase change = 4.66114e-10 + D10, D32, Dmax (mu) = 56.8885, 79.6802, 180.77 + Liquid penetration 95% mass (m) = 0.0129485 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0105534, Final residual = 3.95577e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0327651, Final residual = 1.03148e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000711892, Final residual = 3.86704e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000229527, Final residual = 1.84059e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00032404, Final residual = 2.34121e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000323996, Final residual = 2.35058e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000647849, Final residual = 3.11227e-08, No Iterations 1 +min/max(T) = 806.59, 2729.67 +GAMG: Solving for p, Initial residual = 0.0300888, Final residual = 0.000177212, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.3955e-05, global = 2.32028e-05, cumulative = 0.0106345 +GAMG: Solving for p, Initial residual = 0.000181145, Final residual = 5.04263e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.32754e-05, global = 2.32734e-05, cumulative = 0.0106578 +smoothSolver: Solving for epsilon, Initial residual = 0.000573464, Final residual = 6.9143e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00065947, Final residual = 1.08075e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092602 s +other Time = 0 s +rho Equations = 0.000157 s +U Equations = 0.001044 s +Y Equations = 0.00241839 s +E Equations = 0.000643 s +p Equations = 0.002398 s +calculate parcels = 175.204 s +chemistry correctThermo = 0.002865 s +turbulence correct = 0.001088 s +combustion correct(in Y) = 0.0818086 s +percentage of chemistry = 88.3443 % +percentage of rho/U/Y/E = 4.60291 % +========Time details of each equation======= +rhoEqn Time = 0.00031 s +rhoEqn assamble = 0.000244 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001043 s +UEqn assamble = 0.000624 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000419 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001874 s +YEqn assamble = 0.000642 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000235 s +YEqn correct boundary = 0 s +EEqn Time = 0.00048 s +EEqn assamble = 0.000363 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 250.64 s ClockTime = 251 s +Courant Number mean: 0.00337582 max: 0.0184312 +Time = 0.00193 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21911 + Current mass in system = 1.23801e-09 + Linear momentum = (1.80322e-11 -6.05319e-09 0) + |Linear momentum| = 6.05321e-09 + Linear kinetic energy = 1.59892e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 436.029, 540.2 + Mass transfer phase change = 4.68134e-10 + D10, D32, Dmax (mu) = 56.7621, 79.5421, 181.24 + Liquid penetration 95% mass (m) = 0.0129588 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.011452, Final residual = 4.33087e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0310543, Final residual = 9.93285e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000712901, Final residual = 3.83749e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000230831, Final residual = 1.87683e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000325472, Final residual = 2.38827e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000325414, Final residual = 2.39787e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000654116, Final residual = 3.15877e-08, No Iterations 1 +min/max(T) = 806.601, 2729.52 +GAMG: Solving for p, Initial residual = 0.0325231, Final residual = 0.000204454, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.40955e-05, global = 2.32663e-05, cumulative = 0.010681 +GAMG: Solving for p, Initial residual = 0.000209769, Final residual = 6.83897e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.32787e-05, global = 2.32762e-05, cumulative = 0.0107043 +smoothSolver: Solving for epsilon, Initial residual = 0.000565976, Final residual = 6.84433e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000654294, Final residual = 1.07652e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.109911 s +other Time = 1e-06 s +rho Equations = 0.000199 s +U Equations = 0.001192 s +Y Equations = 0.00225448 s +E Equations = 0.000503 s +p Equations = 0.001957 s +calculate parcels = 175.57 s +chemistry correctThermo = 0.00207 s +turbulence correct = 0.000936 s +combustion correct(in Y) = 0.100551 s +percentage of chemistry = 91.4836 % +percentage of rho/U/Y/E = 3.7744 % +========Time details of each equation======= +rhoEqn Time = 0.000322 s +rhoEqn assamble = 0.000253 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001191 s +UEqn assamble = 0.000689 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000502 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001625 s +YEqn assamble = 0.000569 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000114 s +YEqn correct boundary = 0 s +EEqn Time = 0.000378 s +EEqn assamble = 0.000285 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 251.12 s ClockTime = 252 s +Courant Number mean: 0.00347397 max: 0.0186836 +Time = 0.0019325 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21910 + Current mass in system = 1.23598e-09 + Linear momentum = (1.79359e-11 -6.03075e-09 0) + |Linear momentum| = 6.03078e-09 + Linear kinetic energy = 1.59045e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 436.294, 540.2 + Mass transfer phase change = 4.70165e-10 + D10, D32, Dmax (mu) = 56.631, 79.4022, 181.7 + Liquid penetration 95% mass (m) = 0.0129692 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0100345, Final residual = 3.46279e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0293722, Final residual = 9.47749e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000709494, Final residual = 3.79879e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000228955, Final residual = 1.88339e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00032438, Final residual = 2.39999e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000324323, Final residual = 2.40968e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000657962, Final residual = 3.18578e-08, No Iterations 1 +min/max(T) = 806.612, 2729.37 +GAMG: Solving for p, Initial residual = 0.0351952, Final residual = 0.000177707, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.40664e-05, global = 2.33782e-05, cumulative = 0.0107277 +GAMG: Solving for p, Initial residual = 0.000183763, Final residual = 2.93113e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.3416e-05, global = 2.3415e-05, cumulative = 0.0107511 +smoothSolver: Solving for epsilon, Initial residual = 0.000564077, Final residual = 6.84909e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000652225, Final residual = 1.07973e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.088293 s +other Time = 0 s +rho Equations = 0.000168 s +U Equations = 0.001095 s +Y Equations = 0.0024279 s +E Equations = 0.000607 s +p Equations = 0.0024 s +calculate parcels = 175.829 s +chemistry correctThermo = 0.002928 s +turbulence correct = 0.001071 s +combustion correct(in Y) = 0.0773861 s +percentage of chemistry = 87.6469 % +percentage of rho/U/Y/E = 4.86777 % +========Time details of each equation======= +rhoEqn Time = 0.000327 s +rhoEqn assamble = 0.000259 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001095 s +UEqn assamble = 0.000681 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000414 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001867 s +YEqn assamble = 0.000647 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000231 s +YEqn correct boundary = 0 s +EEqn Time = 0.000448 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 251.46 s ClockTime = 252 s +Courant Number mean: 0.00356897 max: 0.0189915 +Time = 0.001935 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21909 + Current mass in system = 1.23393e-09 + Linear momentum = (1.78348e-11 -6.00802e-09 0) + |Linear momentum| = 6.00804e-09 + Linear kinetic energy = 1.58189e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 436.56, 540.2 + Mass transfer phase change = 4.72211e-10 + D10, D32, Dmax (mu) = 56.4944, 79.2603, 182.145 + Liquid penetration 95% mass (m) = 0.0129797 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00953249, Final residual = 3.27481e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0278834, Final residual = 9.0536e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000707634, Final residual = 3.78954e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000226288, Final residual = 1.89559e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00032264, Final residual = 2.41798e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000322587, Final residual = 2.42771e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000660026, Final residual = 3.2046e-08, No Iterations 1 +min/max(T) = 806.624, 2729.26 +GAMG: Solving for p, Initial residual = 0.0381763, Final residual = 0.000178149, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.41893e-05, global = 2.35332e-05, cumulative = 0.0107746 +GAMG: Solving for p, Initial residual = 0.000185083, Final residual = 2.75792e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.35783e-05, global = 2.35774e-05, cumulative = 0.0107982 +smoothSolver: Solving for epsilon, Initial residual = 0.000563996, Final residual = 6.90574e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000651481, Final residual = 1.0875e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.121668 s +other Time = 0 s +rho Equations = 0.000178 s +U Equations = 0.001318 s +Y Equations = 0.00240624 s +E Equations = 0.000595 s +p Equations = 0.002252 s +calculate parcels = 176.188 s +chemistry correctThermo = 0.002885 s +turbulence correct = 0.001052 s +combustion correct(in Y) = 0.110774 s +percentage of chemistry = 91.0459 % +percentage of rho/U/Y/E = 3.69632 % +========Time details of each equation======= +rhoEqn Time = 0.000327 s +rhoEqn assamble = 0.000258 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001317 s +UEqn assamble = 0.000805 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000512 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001752 s +YEqn assamble = 0.000617 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00017 s +YEqn correct boundary = 0 s +EEqn Time = 0.000444 s +EEqn assamble = 0.000329 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 251.94 s ClockTime = 253 s +Courant Number mean: 0.00366031 max: 0.0194791 +Time = 0.0019375 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21907 + Current mass in system = 1.23187e-09 + Linear momentum = (1.77347e-11 -5.98488e-09 0) + |Linear momentum| = 5.98491e-09 + Linear kinetic energy = 1.57319e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 436.83, 540.2 + Mass transfer phase change = 4.74276e-10 + D10, D32, Dmax (mu) = 56.3967, 79.1175, 182.574 + Liquid penetration 95% mass (m) = 0.0129894 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.009241, Final residual = 2.9838e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0264781, Final residual = 8.66636e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000707768, Final residual = 3.79892e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000223475, Final residual = 1.91006e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000320164, Final residual = 2.442e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000320104, Final residual = 2.45183e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000660786, Final residual = 3.21462e-08, No Iterations 1 +min/max(T) = 806.636, 2729.2 +GAMG: Solving for p, Initial residual = 0.041526, Final residual = 0.000193195, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.44125e-05, global = 2.37695e-05, cumulative = 0.010822 +GAMG: Solving for p, Initial residual = 0.000201885, Final residual = 2.49347e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.38073e-05, global = 2.38066e-05, cumulative = 0.0108458 +smoothSolver: Solving for epsilon, Initial residual = 0.00056386, Final residual = 6.95039e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000650514, Final residual = 1.09394e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.109513 s +other Time = 0 s +rho Equations = 0.000182 s +U Equations = 0.001235 s +Y Equations = 0.00248227 s +E Equations = 0.000598 s +p Equations = 0.001903 s +calculate parcels = 176.555 s +chemistry correctThermo = 0.002602 s +turbulence correct = 0.000845 s +combustion correct(in Y) = 0.0994607 s +percentage of chemistry = 90.8209 % +percentage of rho/U/Y/E = 4.1066 % +========Time details of each equation======= +rhoEqn Time = 0.000331 s +rhoEqn assamble = 0.00026 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001233 s +UEqn assamble = 0.000744 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000489 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001764 s +YEqn assamble = 0.000629 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000135 s +YEqn correct boundary = 0 s +EEqn Time = 0.000443 s +EEqn assamble = 0.000329 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 252.42 s ClockTime = 253 s +Courant Number mean: 0.00374702 max: 0.0198671 +Time = 0.00194 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21906 + Current mass in system = 1.22979e-09 + Linear momentum = (1.76376e-11 -5.96129e-09 0) + |Linear momentum| = 5.96132e-09 + Linear kinetic energy = 1.56433e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 437.103, 540.2 + Mass transfer phase change = 4.76357e-10 + D10, D32, Dmax (mu) = 56.252, 78.9698, 182.783 + Liquid penetration 95% mass (m) = 0.0129984 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00939011, Final residual = 3.21041e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0251187, Final residual = 8.2934e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000703704, Final residual = 3.77292e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000220196, Final residual = 1.92256e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000318271, Final residual = 2.46709e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000318221, Final residual = 2.47704e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000660964, Final residual = 3.23165e-08, No Iterations 1 +min/max(T) = 806.649, 2729.17 +GAMG: Solving for p, Initial residual = 0.0452955, Final residual = 0.000200126, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.4579e-05, global = 2.39305e-05, cumulative = 0.0108697 +GAMG: Solving for p, Initial residual = 0.000210253, Final residual = 2.44731e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.39771e-05, global = 2.39763e-05, cumulative = 0.0108937 +smoothSolver: Solving for epsilon, Initial residual = 0.000564812, Final residual = 7.01051e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000649801, Final residual = 1.10227e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097352 s +other Time = 0 s +rho Equations = 0.000182 s +U Equations = 0.001298 s +Y Equations = 0.00237533 s +E Equations = 0.000625 s +p Equations = 0.00187 s +calculate parcels = 176.896 s +chemistry correctThermo = 0.002521 s +turbulence correct = 0.000849 s +combustion correct(in Y) = 0.0874307 s +percentage of chemistry = 89.8088 % +percentage of rho/U/Y/E = 4.60219 % +========Time details of each equation======= +rhoEqn Time = 0.000304 s +rhoEqn assamble = 0.000238 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001298 s +UEqn assamble = 0.000781 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000517 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001761 s +YEqn assamble = 0.000624 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00019 s +YEqn correct boundary = 0 s +EEqn Time = 0.000457 s +EEqn assamble = 0.000334 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000123 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 252.86 s ClockTime = 253 s +Courant Number mean: 0.00382885 max: 0.0203404 +Time = 0.0019425 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21902 + Current mass in system = 1.22765e-09 + Linear momentum = (1.75366e-11 -5.93708e-09 0) + |Linear momentum| = 5.93711e-09 + Linear kinetic energy = 1.55527e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 437.38, 540.2 + Mass transfer phase change = 4.78493e-10 + D10, D32, Dmax (mu) = 56.1647, 78.8267, 182.558 + Liquid penetration 95% mass (m) = 0.0130075 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0112683, Final residual = 4.00415e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0238044, Final residual = 7.93344e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000702882, Final residual = 3.81273e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000216935, Final residual = 1.93752e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000313497, Final residual = 2.46201e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000313456, Final residual = 2.47198e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000658106, Final residual = 3.20468e-08, No Iterations 1 +min/max(T) = 806.664, 2729.24 +GAMG: Solving for p, Initial residual = 0.0496314, Final residual = 0.000257795, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.51928e-05, global = 2.45628e-05, cumulative = 0.0109183 +GAMG: Solving for p, Initial residual = 0.000268648, Final residual = 9.79221e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.46254e-05, global = 2.46229e-05, cumulative = 0.0109429 +smoothSolver: Solving for epsilon, Initial residual = 0.000567918, Final residual = 7.05817e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00064977, Final residual = 1.10684e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102763 s +other Time = 0 s +rho Equations = 0.000193 s +U Equations = 0.001178 s +Y Equations = 0.00256662 s +E Equations = 0.000602 s +p Equations = 0.002308 s +calculate parcels = 177.252 s +chemistry correctThermo = 0.002882 s +turbulence correct = 0.001034 s +combustion correct(in Y) = 0.0917864 s +percentage of chemistry = 89.3185 % +percentage of rho/U/Y/E = 4.41756 % +========Time details of each equation======= +rhoEqn Time = 0.000359 s +rhoEqn assamble = 0.000268 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001176 s +UEqn assamble = 0.000671 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000505 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001906 s +YEqn assamble = 0.000687 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.0002 s +YEqn correct boundary = 0 s +EEqn Time = 0.000443 s +EEqn assamble = 0.000331 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 253.32 s ClockTime = 254 s +Courant Number mean: 0.00390799 max: 0.0206858 +Time = 0.001945 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21899 + Current mass in system = 1.2255e-09 + Linear momentum = (1.74117e-11 -5.91227e-09 0) + |Linear momentum| = 5.9123e-09 + Linear kinetic energy = 1.54599e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 437.661, 540.2 + Mass transfer phase change = 4.80642e-10 + D10, D32, Dmax (mu) = 56.0565, 78.6774, 182.331 + Liquid penetration 95% mass (m) = 0.0130182 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0167205, Final residual = 7.14667e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0225474, Final residual = 7.56633e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000707074, Final residual = 3.88338e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000213068, Final residual = 1.94381e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000311435, Final residual = 2.49884e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000311385, Final residual = 2.50887e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000657549, Final residual = 3.22243e-08, No Iterations 1 +min/max(T) = 806.683, 2729.23 +GAMG: Solving for p, Initial residual = 0.0539373, Final residual = 0.000305909, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.54875e-05, global = 2.47318e-05, cumulative = 0.0109676 +GAMG: Solving for p, Initial residual = 0.000318453, Final residual = 9.28516e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.47704e-05, global = 2.47682e-05, cumulative = 0.0109924 +smoothSolver: Solving for epsilon, Initial residual = 0.000569889, Final residual = 7.14982e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000650216, Final residual = 1.1186e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.080029 s +other Time = 0 s +rho Equations = 0.000178 s +U Equations = 0.001089 s +Y Equations = 0.00246668 s +E Equations = 0.000552 s +p Equations = 0.002678 s +calculate parcels = 177.55 s +chemistry correctThermo = 0.002001 s +turbulence correct = 0.001002 s +combustion correct(in Y) = 0.0698533 s +percentage of chemistry = 87.285 % +percentage of rho/U/Y/E = 5.35516 % +========Time details of each equation======= +rhoEqn Time = 0.000337 s +rhoEqn assamble = 0.000273 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001088 s +UEqn assamble = 0.000676 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000412 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00191 s +YEqn assamble = 0.000619 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000186 s +YEqn correct boundary = 0 s +EEqn Time = 0.000421 s +EEqn assamble = 0.000319 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000102 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 253.7 s ClockTime = 254 s +Courant Number mean: 0.00398021 max: 0.0210834 +Time = 0.0019475 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21896 + Current mass in system = 1.22329e-09 + Linear momentum = (1.72778e-11 -5.88671e-09 0) + |Linear momentum| = 5.88674e-09 + Linear kinetic energy = 1.53646e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 437.944, 540.2 + Mass transfer phase change = 4.82852e-10 + D10, D32, Dmax (mu) = 55.9222, 78.528, 182.103 + Liquid penetration 95% mass (m) = 0.0130282 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0174623, Final residual = 7.24873e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0212282, Final residual = 7.17599e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000717487, Final residual = 4.1764e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000208701, Final residual = 1.94872e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000310314, Final residual = 2.55248e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000310261, Final residual = 2.56281e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000654194, Final residual = 3.2456e-08, No Iterations 1 +min/max(T) = 806.706, 2729.17 +GAMG: Solving for p, Initial residual = 0.0594334, Final residual = 0.000392553, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.60792e-05, global = 2.54117e-05, cumulative = 0.0110178 +GAMG: Solving for p, Initial residual = 0.000409444, Final residual = 4.12711e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.54781e-05, global = 2.54775e-05, cumulative = 0.0110433 +smoothSolver: Solving for epsilon, Initial residual = 0.000575455, Final residual = 7.21222e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000651727, Final residual = 1.12307e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.108934 s +other Time = 0 s +rho Equations = 0.000175 s +U Equations = 0.001169 s +Y Equations = 0.00310731 s +E Equations = 0.000729 s +p Equations = 0.002802 s +calculate parcels = 177.851 s +chemistry correctThermo = 0.00333 s +turbulence correct = 0.001177 s +combustion correct(in Y) = 0.0961877 s +percentage of chemistry = 88.2991 % +percentage of rho/U/Y/E = 4.75546 % +========Time details of each equation======= +rhoEqn Time = 0.000337 s +rhoEqn assamble = 0.000272 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001168 s +UEqn assamble = 0.000668 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.0005 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002445 s +YEqn assamble = 0.000866 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000289 s +YEqn correct boundary = 0 s +EEqn Time = 0.000541 s +EEqn assamble = 0.00041 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000131 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 254.11 s ClockTime = 255 s +Courant Number mean: 0.00404869 max: 0.0215974 +Time = 0.00195 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21893 + Current mass in system = 1.22107e-09 + Linear momentum = (1.71878e-11 -5.86033e-09 0) + |Linear momentum| = 5.86035e-09 + Linear kinetic energy = 1.52664e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 438.23, 540.2 + Mass transfer phase change = 4.85073e-10 + D10, D32, Dmax (mu) = 55.7723, 78.3701, 181.875 + Liquid penetration 95% mass (m) = 0.0130386 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0227762, Final residual = 1.08846e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0200077, Final residual = 6.81485e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000715301, Final residual = 4.10892e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000203418, Final residual = 1.94503e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000304307, Final residual = 2.55892e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000304241, Final residual = 2.56901e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000651252, Final residual = 3.22909e-08, No Iterations 1 +min/max(T) = 806.734, 2729.09 +GAMG: Solving for p, Initial residual = 0.0648185, Final residual = 0.000388116, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.62882e-05, global = 2.5582e-05, cumulative = 0.0110689 +GAMG: Solving for p, Initial residual = 0.00040169, Final residual = 7.40239e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.55904e-05, global = 2.55891e-05, cumulative = 0.0110944 +smoothSolver: Solving for epsilon, Initial residual = 0.000582757, Final residual = 7.51007e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000656686, Final residual = 1.15273e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094613 s +other Time = 1e-06 s +rho Equations = 0.000151 s +U Equations = 0.001003 s +Y Equations = 0.00241971 s +E Equations = 0.000672 s +p Equations = 0.002921 s +calculate parcels = 178.152 s +chemistry correctThermo = 0.002932 s +turbulence correct = 0.001267 s +combustion correct(in Y) = 0.0830473 s +percentage of chemistry = 87.7758 % +percentage of rho/U/Y/E = 4.48745 % +========Time details of each equation======= +rhoEqn Time = 0.000349 s +rhoEqn assamble = 0.000279 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001001 s +UEqn assamble = 0.000565 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000436 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001858 s +YEqn assamble = 0.000633 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000234 s +YEqn correct boundary = 0 s +EEqn Time = 0.000511 s +EEqn assamble = 0.000386 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000125 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 254.5 s ClockTime = 255 s +Courant Number mean: 0.00411134 max: 0.0221564 +Time = 0.0019525 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21888 + Current mass in system = 1.21881e-09 + Linear momentum = (1.71612e-11 -5.833e-09 0) + |Linear momentum| = 5.83303e-09 + Linear kinetic energy = 1.5165e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 438.521, 540.2 + Mass transfer phase change = 4.8733e-10 + D10, D32, Dmax (mu) = 55.6805, 78.2113, 181.646 + Liquid penetration 95% mass (m) = 0.0130478 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0231881, Final residual = 1.10896e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0187943, Final residual = 6.52546e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000718067, Final residual = 3.82336e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000198889, Final residual = 1.93536e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000297177, Final residual = 2.51838e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000297113, Final residual = 2.5283e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000645018, Final residual = 3.11195e-08, No Iterations 1 +min/max(T) = 806.767, 2729.06 +GAMG: Solving for p, Initial residual = 0.0720521, Final residual = 0.000539259, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.681e-05, global = 2.60379e-05, cumulative = 0.0111205 +GAMG: Solving for p, Initial residual = 0.000556472, Final residual = 5.22762e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.60194e-05, global = 2.60185e-05, cumulative = 0.0111465 +smoothSolver: Solving for epsilon, Initial residual = 0.000581833, Final residual = 7.70749e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000657247, Final residual = 1.17086e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.108285 s +other Time = 0 s +rho Equations = 0.000186 s +U Equations = 0.001215 s +Y Equations = 0.00359118 s +E Equations = 0.00096 s +p Equations = 0.002007 s +calculate parcels = 178.494 s +chemistry correctThermo = 0.004243 s +turbulence correct = 0.000859 s +combustion correct(in Y) = 0.0950128 s +percentage of chemistry = 87.7433 % +percentage of rho/U/Y/E = 5.49677 % +========Time details of each equation======= +rhoEqn Time = 0.000301 s +rhoEqn assamble = 0.000239 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001214 s +UEqn assamble = 0.00071 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000504 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002941 s +YEqn assamble = 0.001008 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000527 s +YEqn correct boundary = 0 s +EEqn Time = 0.000724 s +EEqn assamble = 0.000531 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000193 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 254.95 s ClockTime = 256 s +Courant Number mean: 0.00416718 max: 0.0226156 +Time = 0.001955 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21880 + Current mass in system = 1.21648e-09 + Linear momentum = (1.71376e-11 -5.80469e-09 0) + |Linear momentum| = 5.80471e-09 + Linear kinetic energy = 1.50602e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 438.815, 540.2 + Mass transfer phase change = 4.89658e-10 + D10, D32, Dmax (mu) = 55.67, 78.052, 181.408 + Liquid penetration 95% mass (m) = 0.0130575 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0253318, Final residual = 1.13527e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0185691, Final residual = 6.573e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000728908, Final residual = 4.20013e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000195108, Final residual = 1.92382e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000294049, Final residual = 2.5613e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000293985, Final residual = 2.57135e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000636252, Final residual = 3.1586e-08, No Iterations 1 +min/max(T) = 806.802, 2729.08 +GAMG: Solving for p, Initial residual = 0.0802919, Final residual = 0.00079207, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.79432e-05, global = 2.67884e-05, cumulative = 0.0111733 +GAMG: Solving for p, Initial residual = 0.000833107, Final residual = 2.51939e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.68319e-05, global = 2.68315e-05, cumulative = 0.0112001 +smoothSolver: Solving for epsilon, Initial residual = 0.000589895, Final residual = 7.77093e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000659815, Final residual = 1.17409e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.089493 s +other Time = 0 s +rho Equations = 0.000155 s +U Equations = 0.001022 s +Y Equations = 0.00227086 s +E Equations = 0.000498 s +p Equations = 0.002162 s +calculate parcels = 178.841 s +chemistry correctThermo = 0.002025 s +turbulence correct = 0.000896 s +combustion correct(in Y) = 0.0802841 s +percentage of chemistry = 89.71 % +percentage of rho/U/Y/E = 4.40913 % +========Time details of each equation======= +rhoEqn Time = 0.000275 s +rhoEqn assamble = 0.000217 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00102 s +UEqn assamble = 0.000609 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000411 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001721 s +YEqn assamble = 0.000595 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00019 s +YEqn correct boundary = 0 s +EEqn Time = 0.000374 s +EEqn assamble = 0.000278 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 255.39 s ClockTime = 256 s +Courant Number mean: 0.00421919 max: 0.0231733 +Time = 0.0019575 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21878 + Current mass in system = 1.21421e-09 + Linear momentum = (1.70369e-11 -5.77554e-09 0) + |Linear momentum| = 5.77557e-09 + Linear kinetic energy = 1.49523e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 439.115, 540.2 + Mass transfer phase change = 4.91936e-10 + D10, D32, Dmax (mu) = 55.499, 77.8741, 181.47 + Liquid penetration 95% mass (m) = 0.0130672 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0325334, Final residual = 1.68211e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0187753, Final residual = 6.86895e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000701023, Final residual = 3.8188e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000193279, Final residual = 1.927e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000288282, Final residual = 2.56792e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000288197, Final residual = 2.57783e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000628245, Final residual = 3.15934e-08, No Iterations 1 +min/max(T) = 806.84, 2729.07 +GAMG: Solving for p, Initial residual = 0.0884255, Final residual = 0.00100617, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.74073e-05, global = 2.63146e-05, cumulative = 0.0112264 +GAMG: Solving for p, Initial residual = 0.00103735, Final residual = 2.7477e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.62549e-05, global = 2.62546e-05, cumulative = 0.0112527 +smoothSolver: Solving for epsilon, Initial residual = 0.000588577, Final residual = 7.92023e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000659508, Final residual = 1.18878e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.101317 s +other Time = 0 s +rho Equations = 0.000208 s +U Equations = 0.001402 s +Y Equations = 0.00254303 s +E Equations = 0.000616 s +p Equations = 0.002764 s +calculate parcels = 179.168 s +chemistry correctThermo = 0.002892 s +turbulence correct = 0.001086 s +combustion correct(in Y) = 0.089572 s +percentage of chemistry = 88.4076 % +percentage of rho/U/Y/E = 4.70704 % +========Time details of each equation======= +rhoEqn Time = 0.000359 s +rhoEqn assamble = 0.000286 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001399 s +UEqn assamble = 0.000843 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000556 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001855 s +YEqn assamble = 0.00065 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000197 s +YEqn correct boundary = 0 s +EEqn Time = 0.000452 s +EEqn assamble = 0.00034 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 255.82 s ClockTime = 256 s +Courant Number mean: 0.00426191 max: 0.0236723 +Time = 0.00196 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21870 + Current mass in system = 1.21184e-09 + Linear momentum = (1.68915e-11 -5.74549e-09 0) + |Linear momentum| = 5.74551e-09 + Linear kinetic energy = 1.48416e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 439.418, 540.2 + Mass transfer phase change = 4.94308e-10 + D10, D32, Dmax (mu) = 55.4502, 77.7034, 181.251 + Liquid penetration 95% mass (m) = 0.0130765 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0254154, Final residual = 1.24351e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0190178, Final residual = 7.08887e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000735032, Final residual = 4.08952e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000188332, Final residual = 1.90925e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000286006, Final residual = 2.55651e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000285919, Final residual = 2.56641e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000624589, Final residual = 3.18177e-08, No Iterations 1 +min/max(T) = 806.881, 2729.1 +GAMG: Solving for p, Initial residual = 0.0999994, Final residual = 0.00102798, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.82275e-05, global = 2.73372e-05, cumulative = 0.01128 +GAMG: Solving for p, Initial residual = 0.00107113, Final residual = 2.76583e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.73364e-05, global = 2.73361e-05, cumulative = 0.0113074 +smoothSolver: Solving for epsilon, Initial residual = 0.000597481, Final residual = 8.0076e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000660431, Final residual = 1.19011e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.083829 s +other Time = 1e-06 s +rho Equations = 0.000169 s +U Equations = 0.001113 s +Y Equations = 0.00277632 s +E Equations = 0.000827 s +p Equations = 0.00228 s +calculate parcels = 179.452 s +chemistry correctThermo = 0.001958 s +turbulence correct = 0.000831 s +combustion correct(in Y) = 0.0736417 s +percentage of chemistry = 87.8475 % +percentage of rho/U/Y/E = 5.82772 % +========Time details of each equation======= +rhoEqn Time = 0.000301 s +rhoEqn assamble = 0.000244 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001112 s +UEqn assamble = 0.000691 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000421 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00221 s +YEqn assamble = 0.000743 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000299 s +YEqn correct boundary = 0 s +EEqn Time = 0.000652 s +EEqn assamble = 0.000358 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000294 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 256.18 s ClockTime = 257 s +Courant Number mean: 0.0043 max: 0.0239021 +Time = 0.0019625 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21867 + Current mass in system = 1.20949e-09 + Linear momentum = (1.68072e-11 -5.71477e-09 0) + |Linear momentum| = 5.71479e-09 + Linear kinetic energy = 1.47285e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 439.706, 540.2 + Mass transfer phase change = 4.96648e-10 + D10, D32, Dmax (mu) = 55.2711, 77.5168, 181.031 + Liquid penetration 95% mass (m) = 0.0130852 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0290845, Final residual = 1.64612e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0195012, Final residual = 7.33201e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000694053, Final residual = 3.83509e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000184734, Final residual = 1.89569e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000278562, Final residual = 2.51265e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000278472, Final residual = 2.52229e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000611541, Final residual = 3.05968e-08, No Iterations 1 +min/max(T) = 806.922, 2729.21 +GAMG: Solving for p, Initial residual = 0.1127, Final residual = 0.00133321, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.83382e-05, global = 2.70631e-05, cumulative = 0.0113344 +GAMG: Solving for p, Initial residual = 0.00138041, Final residual = 2.96513e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.69729e-05, global = 2.69726e-05, cumulative = 0.0113614 +smoothSolver: Solving for epsilon, Initial residual = 0.000602885, Final residual = 8.32071e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000662989, Final residual = 1.21587e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09471 s +other Time = 0 s +rho Equations = 0.000179 s +U Equations = 0.001269 s +Y Equations = 0.00246535 s +E Equations = 0.000605 s +p Equations = 0.002608 s +calculate parcels = 179.772 s +chemistry correctThermo = 0.00284 s +turbulence correct = 0.000977 s +combustion correct(in Y) = 0.0835706 s +percentage of chemistry = 88.2385 % +percentage of rho/U/Y/E = 4.77072 % +========Time details of each equation======= +rhoEqn Time = 0.000342 s +rhoEqn assamble = 0.000269 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001269 s +UEqn assamble = 0.000771 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000498 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001826 s +YEqn assamble = 0.000649 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000194 s +YEqn correct boundary = 0 s +EEqn Time = 0.000448 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 256.6 s ClockTime = 257 s +Courant Number mean: 0.00433147 max: 0.0240842 +Time = 0.001965 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21858 + Current mass in system = 1.20704e-09 + Linear momentum = (1.67633e-11 -5.6831e-09 0) + |Linear momentum| = 5.68313e-09 + Linear kinetic energy = 1.46127e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 439.913, 540.2 + Mass transfer phase change = 4.99105e-10 + D10, D32, Dmax (mu) = 55.2381, 77.3435, 180.809 + Liquid penetration 95% mass (m) = 0.0130942 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0211928, Final residual = 1.02253e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0197904, Final residual = 7.56178e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000721684, Final residual = 4.20999e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000181376, Final residual = 1.87808e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000274441, Final residual = 2.51596e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000274354, Final residual = 2.52598e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000606464, Final residual = 3.09214e-08, No Iterations 1 +min/max(T) = 806.967, 2729.29 +GAMG: Solving for p, Initial residual = 0.119851, Final residual = 0.00104439, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.9044e-05, global = 2.83231e-05, cumulative = 0.0113897 +GAMG: Solving for p, Initial residual = 0.00102187, Final residual = 9.16847e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.83218e-05, global = 2.83209e-05, cumulative = 0.011418 +smoothSolver: Solving for epsilon, Initial residual = 0.000605088, Final residual = 8.37305e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000661322, Final residual = 1.21184e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.108829 s +other Time = 1e-06 s +rho Equations = 0.000193 s +U Equations = 0.001116 s +Y Equations = 0.00243186 s +E Equations = 0.000621 s +p Equations = 0.002581 s +calculate parcels = 180.106 s +chemistry correctThermo = 0.002875 s +turbulence correct = 0.001104 s +combustion correct(in Y) = 0.0977051 s +percentage of chemistry = 89.7786 % +percentage of rho/U/Y/E = 4.00799 % +========Time details of each equation======= +rhoEqn Time = 0.000345 s +rhoEqn assamble = 0.000271 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001115 s +UEqn assamble = 0.000667 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000448 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001799 s +YEqn assamble = 0.000646 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000185 s +YEqn correct boundary = 0 s +EEqn Time = 0.000461 s +EEqn assamble = 0.000344 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 257.04 s ClockTime = 258 s +Courant Number mean: 0.00436053 max: 0.0244212 +Time = 0.0019675 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21856 + Current mass in system = 1.20465e-09 + Linear momentum = (1.67638e-11 -5.65073e-09 0) + |Linear momentum| = 5.65076e-09 + Linear kinetic energy = 1.44944e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 440.122, 540.2 + Mass transfer phase change = 5.01496e-10 + D10, D32, Dmax (mu) = 55.0164, 77.1447, 180.583 + Liquid penetration 95% mass (m) = 0.0131036 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0215401, Final residual = 1.1027e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0201431, Final residual = 7.73132e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000699967, Final residual = 4.10659e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000178594, Final residual = 1.85996e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000272697, Final residual = 2.54262e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000272585, Final residual = 2.55242e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000599802, Final residual = 3.13677e-08, No Iterations 1 +min/max(T) = 807.016, 2729.26 +GAMG: Solving for p, Initial residual = 0.115766, Final residual = 0.00113251, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.88411e-05, global = 2.76195e-05, cumulative = 0.0114457 +GAMG: Solving for p, Initial residual = 0.00106846, Final residual = 9.32293e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.75546e-05, global = 2.75536e-05, cumulative = 0.0114732 +smoothSolver: Solving for epsilon, Initial residual = 0.000621996, Final residual = 8.81246e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000670655, Final residual = 1.25053e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.104195 s +other Time = 1e-06 s +rho Equations = 0.000157 s +U Equations = 0.00099 s +Y Equations = 0.00236809 s +E Equations = 0.000597 s +p Equations = 0.002393 s +calculate parcels = 180.479 s +chemistry correctThermo = 0.002879 s +turbulence correct = 0.001113 s +combustion correct(in Y) = 0.0934999 s +percentage of chemistry = 89.7355 % +percentage of rho/U/Y/E = 3.94653 % +========Time details of each equation======= +rhoEqn Time = 0.000295 s +rhoEqn assamble = 0.000234 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000989 s +UEqn assamble = 0.000577 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000412 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00182 s +YEqn assamble = 0.000627 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000245 s +YEqn correct boundary = 0 s +EEqn Time = 0.000448 s +EEqn assamble = 0.000322 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000126 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 257.52 s ClockTime = 258 s +Courant Number mean: 0.00437772 max: 0.0246872 +Time = 0.00197 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21851 + Current mass in system = 1.20215e-09 + Linear momentum = (1.67658e-11 -5.6176e-09 0) + |Linear momentum| = 5.61762e-09 + Linear kinetic energy = 1.43741e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 440.33, 540.2 + Mass transfer phase change = 5.03988e-10 + D10, D32, Dmax (mu) = 54.8316, 76.9527, 180.356 + Liquid penetration 95% mass (m) = 0.0131133 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0185697, Final residual = 8.79702e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0204136, Final residual = 7.97844e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000722524, Final residual = 4.56671e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000175853, Final residual = 1.84638e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000272219, Final residual = 2.58354e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000272122, Final residual = 2.59373e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000590591, Final residual = 3.10075e-08, No Iterations 1 +min/max(T) = 807.07, 2729.2 +GAMG: Solving for p, Initial residual = 0.112131, Final residual = 0.000951212, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.946e-05, global = 2.87089e-05, cumulative = 0.0115019 +GAMG: Solving for p, Initial residual = 0.000895256, Final residual = 2.22687e-07, No Iterations 5 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.87251e-05, global = 2.87249e-05, cumulative = 0.0115307 +smoothSolver: Solving for epsilon, Initial residual = 0.000624857, Final residual = 8.77408e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000667334, Final residual = 1.2302e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.090461 s +other Time = 1e-06 s +rho Equations = 0.000177 s +U Equations = 0.001284 s +Y Equations = 0.0020985 s +E Equations = 0.000506 s +p Equations = 0.002317 s +calculate parcels = 180.813 s +chemistry correctThermo = 0.002055 s +turbulence correct = 0.000925 s +combustion correct(in Y) = 0.0808945 s +percentage of chemistry = 89.4247 % +percentage of rho/U/Y/E = 4.4942 % +========Time details of each equation======= +rhoEqn Time = 0.000302 s +rhoEqn assamble = 0.000242 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001284 s +UEqn assamble = 0.000757 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000527 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001451 s +YEqn assamble = 0.000532 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.0001 s +YEqn correct boundary = 0 s +EEqn Time = 0.000388 s +EEqn assamble = 0.000292 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 257.94 s ClockTime = 259 s +Courant Number mean: 0.00439037 max: 0.0247344 +Time = 0.0019725 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21849 + Current mass in system = 1.19972e-09 + Linear momentum = (1.67191e-11 -5.58393e-09 0) + |Linear momentum| = 5.58395e-09 + Linear kinetic energy = 1.4252e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 440.539, 540.2 + Mass transfer phase change = 5.06419e-10 + D10, D32, Dmax (mu) = 54.6069, 76.7454, 180.128 + Liquid penetration 95% mass (m) = 0.0131232 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0194563, Final residual = 1.13839e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0206949, Final residual = 8.0862e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000692145, Final residual = 4.00699e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000174469, Final residual = 1.83442e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000265755, Final residual = 2.49108e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000265648, Final residual = 2.50103e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000587354, Final residual = 3.03645e-08, No Iterations 1 +min/max(T) = 807.13, 2729.15 +GAMG: Solving for p, Initial residual = 0.103778, Final residual = 0.00109333, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.93506e-05, global = 2.81839e-05, cumulative = 0.0115588 +GAMG: Solving for p, Initial residual = 0.00103247, Final residual = 5.87103e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.80252e-05, global = 2.80244e-05, cumulative = 0.0115869 +smoothSolver: Solving for epsilon, Initial residual = 0.000641428, Final residual = 9.21123e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000677119, Final residual = 1.27502e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094228 s +other Time = 0 s +rho Equations = 0.000199 s +U Equations = 0.001194 s +Y Equations = 0.00227813 s +E Equations = 0.000502 s +p Equations = 0.00209 s +calculate parcels = 181.143 s +chemistry correctThermo = 0.002113 s +turbulence correct = 0.000968 s +combustion correct(in Y) = 0.0846759 s +percentage of chemistry = 89.8627 % +percentage of rho/U/Y/E = 4.42876 % +========Time details of each equation======= +rhoEqn Time = 0.000325 s +rhoEqn assamble = 0.000246 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001193 s +UEqn assamble = 0.000692 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000501 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001628 s +YEqn assamble = 0.000563 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000112 s +YEqn correct boundary = 0 s +EEqn Time = 0.000377 s +EEqn assamble = 0.000282 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 258.37 s ClockTime = 259 s +Courant Number mean: 0.00439157 max: 0.024716 +Time = 0.001975 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21844 + Current mass in system = 1.19726e-09 + Linear momentum = (1.6638e-11 -5.54961e-09 0) + |Linear momentum| = 5.54963e-09 + Linear kinetic energy = 1.41283e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 440.749, 540.2 + Mass transfer phase change = 5.08883e-10 + D10, D32, Dmax (mu) = 54.4584, 76.5407, 180.163 + Liquid penetration 95% mass (m) = 0.0131325 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0175167, Final residual = 8.50794e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0206186, Final residual = 8.01756e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000702394, Final residual = 4.11947e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000171866, Final residual = 1.82406e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000260149, Final residual = 2.48821e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000260022, Final residual = 2.49799e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000581184, Final residual = 3.07921e-08, No Iterations 1 +min/max(T) = 807.195, 2729.15 +GAMG: Solving for p, Initial residual = 0.0983679, Final residual = 0.000803785, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.93279e-05, global = 2.84903e-05, cumulative = 0.0116153 +GAMG: Solving for p, Initial residual = 0.000768779, Final residual = 5.91008e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.83894e-05, global = 2.83888e-05, cumulative = 0.0116437 +smoothSolver: Solving for epsilon, Initial residual = 0.00064374, Final residual = 9.33238e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000675096, Final residual = 1.27889e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.079969 s +other Time = 0 s +rho Equations = 0.000165 s +U Equations = 0.001194 s +Y Equations = 0.00210071 s +E Equations = 0.000479 s +p Equations = 0.001935 s +calculate parcels = 181.398 s +chemistry correctThermo = 0.001974 s +turbulence correct = 0.00084 s +combustion correct(in Y) = 0.0710923 s +percentage of chemistry = 88.8998 % +percentage of rho/U/Y/E = 4.92529 % +========Time details of each equation======= +rhoEqn Time = 0.000278 s +rhoEqn assamble = 0.000221 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001192 s +UEqn assamble = 0.000698 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000494 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001491 s +YEqn assamble = 0.000534 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000107 s +YEqn correct boundary = 0 s +EEqn Time = 0.000362 s +EEqn assamble = 0.000269 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 258.7 s ClockTime = 259 s +Courant Number mean: 0.00438247 max: 0.0247199 +Time = 0.0019775 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21843 + Current mass in system = 1.19482e-09 + Linear momentum = (1.6515e-11 -5.51501e-09 0) + |Linear momentum| = 5.51503e-09 + Linear kinetic energy = 1.4004e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 440.961, 540.2 + Mass transfer phase change = 5.11322e-10 + D10, D32, Dmax (mu) = 54.2054, 76.323, 180.463 + Liquid penetration 95% mass (m) = 0.0131428 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0170096, Final residual = 7.40173e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0205652, Final residual = 7.89029e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000673583, Final residual = 3.96763e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000168638, Final residual = 1.81794e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000259698, Final residual = 2.50816e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000259568, Final residual = 2.51789e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00056886, Final residual = 3.03653e-08, No Iterations 1 +min/max(T) = 807.205, 2729.23 +GAMG: Solving for p, Initial residual = 0.0914395, Final residual = 0.000792674, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.91844e-05, global = 2.81946e-05, cumulative = 0.0116719 +GAMG: Solving for p, Initial residual = 0.000748784, Final residual = 2.97492e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.81121e-05, global = 2.81118e-05, cumulative = 0.0117 +smoothSolver: Solving for epsilon, Initial residual = 0.000644136, Final residual = 9.37442e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000673439, Final residual = 1.27722e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.114487 s +other Time = 0 s +rho Equations = 0.000303 s +U Equations = 0.001806 s +Y Equations = 0.00303742 s +E Equations = 0.000673 s +p Equations = 0.00331 s +calculate parcels = 181.74 s +chemistry correctThermo = 0.002956 s +turbulence correct = 0.001345 s +combustion correct(in Y) = 0.100732 s +percentage of chemistry = 87.9852 % +percentage of rho/U/Y/E = 5.08304 % +========Time details of each equation======= +rhoEqn Time = 0.000522 s +rhoEqn assamble = 0.000403 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000119 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001802 s +UEqn assamble = 0.001084 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000718 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002064 s +YEqn assamble = 0.000752 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 7.2e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000487 s +EEqn assamble = 0.000368 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000119 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 259.16 s ClockTime = 260 s +Courant Number mean: 0.00436353 max: 0.0246493 +Time = 0.00198 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21841 + Current mass in system = 1.19236e-09 + Linear momentum = (1.63648e-11 -5.48032e-09 0) + |Linear momentum| = 5.48035e-09 + Linear kinetic energy = 1.38799e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 441.174, 540.2 + Mass transfer phase change = 5.13786e-10 + D10, D32, Dmax (mu) = 53.9477, 76.1061, 180.742 + Liquid penetration 95% mass (m) = 0.0131518 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0156249, Final residual = 6.92853e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0201393, Final residual = 7.57077e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000672282, Final residual = 3.97155e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000166854, Final residual = 1.816e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000256615, Final residual = 2.50444e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000256496, Final residual = 2.51455e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000562742, Final residual = 3.02821e-08, No Iterations 1 +min/max(T) = 807.159, 2729.33 +GAMG: Solving for p, Initial residual = 0.0844143, Final residual = 0.000692069, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.92796e-05, global = 2.84564e-05, cumulative = 0.0117285 +GAMG: Solving for p, Initial residual = 0.000649712, Final residual = 2.78088e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.83993e-05, global = 2.8399e-05, cumulative = 0.0117569 +smoothSolver: Solving for epsilon, Initial residual = 0.000638984, Final residual = 9.29249e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.0006681, Final residual = 1.2621e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.116179 s +other Time = 0 s +rho Equations = 0.000306 s +U Equations = 0.001611 s +Y Equations = 0.00287403 s +E Equations = 0.000564 s +p Equations = 0.003463 s +calculate parcels = 182.133 s +chemistry correctThermo = 0.002124 s +turbulence correct = 0.001305 s +combustion correct(in Y) = 0.103657 s +percentage of chemistry = 89.2218 % +percentage of rho/U/Y/E = 4.60929 % +========Time details of each equation======= +rhoEqn Time = 0.000542 s +rhoEqn assamble = 0.000432 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.00011 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00161 s +UEqn assamble = 0.001014 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000596 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002101 s +YEqn assamble = 0.000731 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.9e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000408 s +EEqn assamble = 0.000308 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.0001 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 259.67 s ClockTime = 260 s +Courant Number mean: 0.00433794 max: 0.0242802 +Time = 0.0019825 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21840 + Current mass in system = 1.18989e-09 + Linear momentum = (1.62402e-11 -5.44576e-09 0) + |Linear momentum| = 5.44579e-09 + Linear kinetic energy = 1.3757e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 441.389, 540.2 + Mass transfer phase change = 5.16253e-10 + D10, D32, Dmax (mu) = 53.7062, 75.8898, 181.085 + Liquid penetration 95% mass (m) = 0.0131597 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0160974, Final residual = 7.34384e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0196219, Final residual = 7.1561e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00067529, Final residual = 4.13136e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000166392, Final residual = 1.81629e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000256877, Final residual = 2.51106e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000256784, Final residual = 2.52114e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000561984, Final residual = 3.06207e-08, No Iterations 1 +min/max(T) = 807.113, 2729.38 +GAMG: Solving for p, Initial residual = 0.0760212, Final residual = 0.000716278, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.94295e-05, global = 2.85463e-05, cumulative = 0.0117854 +GAMG: Solving for p, Initial residual = 0.000657399, Final residual = 4.39792e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.84389e-05, global = 2.84382e-05, cumulative = 0.0118139 +smoothSolver: Solving for epsilon, Initial residual = 0.000637173, Final residual = 9.299e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00066614, Final residual = 1.25767e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103613 s +other Time = 0 s +rho Equations = 0.000185 s +U Equations = 0.001175 s +Y Equations = 0.00265602 s +E Equations = 0.000685 s +p Equations = 0.003028 s +calculate parcels = 182.534 s +chemistry correctThermo = 0.002914 s +turbulence correct = 0.001219 s +combustion correct(in Y) = 0.091527 s +percentage of chemistry = 88.3354 % +percentage of rho/U/Y/E = 4.5371 % +========Time details of each equation======= +rhoEqn Time = 0.000399 s +rhoEqn assamble = 0.000298 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000101 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001175 s +UEqn assamble = 0.000677 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000498 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00197 s +YEqn assamble = 0.000702 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000188 s +YEqn correct boundary = 0 s +EEqn Time = 0.000513 s +EEqn assamble = 0.000387 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000126 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 260.18 s ClockTime = 261 s +Courant Number mean: 0.00430485 max: 0.0238178 +Time = 0.001985 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21839 + Current mass in system = 1.18741e-09 + Linear momentum = (1.61642e-11 -5.41137e-09 0) + |Linear momentum| = 5.4114e-09 + Linear kinetic energy = 1.36353e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 441.605, 540.2 + Mass transfer phase change = 5.1873e-10 + D10, D32, Dmax (mu) = 53.4557, 75.6732, 181.417 + Liquid penetration 95% mass (m) = 0.0131682 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0167338, Final residual = 7.87974e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0188727, Final residual = 6.62987e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000674802, Final residual = 4.11532e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000166707, Final residual = 1.82535e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000257786, Final residual = 2.55104e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000257704, Final residual = 2.56131e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000563649, Final residual = 3.0783e-08, No Iterations 1 +min/max(T) = 807.067, 2729.38 +GAMG: Solving for p, Initial residual = 0.0678878, Final residual = 0.000502625, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.94159e-05, global = 2.86164e-05, cumulative = 0.0118425 +GAMG: Solving for p, Initial residual = 0.00046748, Final residual = 6.78006e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.85477e-05, global = 2.85463e-05, cumulative = 0.011871 +smoothSolver: Solving for epsilon, Initial residual = 0.000633209, Final residual = 9.30616e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000664943, Final residual = 1.25433e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.117583 s +other Time = 0 s +rho Equations = 0.000181 s +U Equations = 0.001231 s +Y Equations = 0.00253555 s +E Equations = 0.000609 s +p Equations = 0.002282 s +calculate parcels = 182.891 s +chemistry correctThermo = 0.002967 s +turbulence correct = 0.000978 s +combustion correct(in Y) = 0.106575 s +percentage of chemistry = 90.6385 % +percentage of rho/U/Y/E = 3.87518 % +========Time details of each equation======= +rhoEqn Time = 0.00033 s +rhoEqn assamble = 0.000261 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001229 s +UEqn assamble = 0.000699 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00053 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001878 s +YEqn assamble = 0.000645 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000205 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 260.65 s ClockTime = 261 s +Courant Number mean: 0.00426431 max: 0.0234602 +Time = 0.0019875 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21838 + Current mass in system = 1.18494e-09 + Linear momentum = (1.61324e-11 -5.37712e-09 0) + |Linear momentum| = 5.37714e-09 + Linear kinetic energy = 1.35148e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 441.82, 540.2 + Mass transfer phase change = 5.21203e-10 + D10, D32, Dmax (mu) = 53.2039, 75.4547, 181.737 + Liquid penetration 95% mass (m) = 0.0131765 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0172128, Final residual = 7.85491e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0180153, Final residual = 6.09433e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000670118, Final residual = 4.08558e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000167738, Final residual = 1.84605e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000259309, Final residual = 2.59687e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000259234, Final residual = 2.60726e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000564227, Final residual = 3.08837e-08, No Iterations 1 +min/max(T) = 807.022, 2729.39 +GAMG: Solving for p, Initial residual = 0.0610377, Final residual = 0.000459324, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.94498e-05, global = 2.85653e-05, cumulative = 0.0118996 +GAMG: Solving for p, Initial residual = 0.000427275, Final residual = 8.77876e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.851e-05, global = 2.85082e-05, cumulative = 0.0119281 +smoothSolver: Solving for epsilon, Initial residual = 0.000632207, Final residual = 9.33166e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000663832, Final residual = 1.2545e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.07765 s +other Time = 1e-06 s +rho Equations = 0.000174 s +U Equations = 0.001106 s +Y Equations = 0.0023147 s +E Equations = 0.000499 s +p Equations = 0.001953 s +calculate parcels = 183.173 s +chemistry correctThermo = 0.002157 s +turbulence correct = 0.000947 s +combustion correct(in Y) = 0.0682993 s +percentage of chemistry = 87.9579 % +percentage of rho/U/Y/E = 5.27199 % +========Time details of each equation======= +rhoEqn Time = 0.00031 s +rhoEqn assamble = 0.000242 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001105 s +UEqn assamble = 0.000683 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000422 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001734 s +YEqn assamble = 0.000553 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000165 s +YEqn correct boundary = 0 s +EEqn Time = 0.000374 s +EEqn assamble = 0.000282 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 261.01 s ClockTime = 262 s +Courant Number mean: 0.00421562 max: 0.0232964 +Time = 0.00199 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21836 + Current mass in system = 1.18241e-09 + Linear momentum = (1.61115e-11 -5.34305e-09 0) + |Linear momentum| = 5.34308e-09 + Linear kinetic energy = 1.33958e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 442.036, 540.2 + Mass transfer phase change = 5.2373e-10 + D10, D32, Dmax (mu) = 52.949, 75.2398, 182.043 + Liquid penetration 95% mass (m) = 0.0131854 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0157757, Final residual = 6.72017e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.017629, Final residual = 5.86233e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000694404, Final residual = 4.4967e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000168097, Final residual = 1.86439e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000264608, Final residual = 2.67979e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000264527, Final residual = 2.69074e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000568675, Final residual = 3.16774e-08, No Iterations 1 +min/max(T) = 806.978, 2729.44 +GAMG: Solving for p, Initial residual = 0.0560196, Final residual = 0.000499035, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 3.02171e-05, global = 2.91041e-05, cumulative = 0.0119572 +GAMG: Solving for p, Initial residual = 0.000468528, Final residual = 3.74047e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.91198e-05, global = 2.91188e-05, cumulative = 0.0119863 +smoothSolver: Solving for epsilon, Initial residual = 0.000626637, Final residual = 9.12692e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000660382, Final residual = 1.23175e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.123015 s +other Time = 0 s +rho Equations = 0.000288 s +U Equations = 0.001951 s +Y Equations = 0.00284965 s +E Equations = 0.000595 s +p Equations = 0.002467 s +calculate parcels = 183.503 s +chemistry correctThermo = 0.002857 s +turbulence correct = 0.001059 s +combustion correct(in Y) = 0.110689 s +percentage of chemistry = 89.9804 % +percentage of rho/U/Y/E = 4.62029 % +========Time details of each equation======= +rhoEqn Time = 0.00045 s +rhoEqn assamble = 0.00033 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.00012 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001949 s +UEqn assamble = 0.00114 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000809 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001754 s +YEqn assamble = 0.000685 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -1.1e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000434 s +EEqn assamble = 0.000323 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 261.46 s ClockTime = 262 s +Courant Number mean: 0.00416087 max: 0.0244293 +Time = 0.0019925 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21836 + Current mass in system = 1.17994e-09 + Linear momentum = (1.60425e-11 -5.30927e-09 0) + |Linear momentum| = 5.30929e-09 + Linear kinetic energy = 1.32785e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 442.251, 540.2 + Mass transfer phase change = 5.26206e-10 + D10, D32, Dmax (mu) = 52.6741, 75.0208, 182.128 + Liquid penetration 95% mass (m) = 0.0131942 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0195625, Final residual = 1.13051e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0200591, Final residual = 6.78757e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000663448, Final residual = 4.05203e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000169745, Final residual = 1.89992e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000261949, Final residual = 2.66767e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000261857, Final residual = 2.67847e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000563912, Final residual = 3.09193e-08, No Iterations 1 +min/max(T) = 806.936, 2729.54 +GAMG: Solving for p, Initial residual = 0.0509253, Final residual = 0.00053991, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.96861e-05, global = 2.86468e-05, cumulative = 0.012015 +GAMG: Solving for p, Initial residual = 0.000522645, Final residual = 4.31949e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.85476e-05, global = 2.85468e-05, cumulative = 0.0120435 +smoothSolver: Solving for epsilon, Initial residual = 0.000623952, Final residual = 9.17814e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000659076, Final residual = 1.23615e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.099774 s +other Time = 1e-06 s +rho Equations = 0.000236 s +U Equations = 0.001306 s +Y Equations = 0.00215528 s +E Equations = 0.000508 s +p Equations = 0.002038 s +calculate parcels = 183.849 s +chemistry correctThermo = 0.002054 s +turbulence correct = 0.000846 s +combustion correct(in Y) = 0.0903217 s +percentage of chemistry = 90.5263 % +percentage of rho/U/Y/E = 4.2148 % +========Time details of each equation======= +rhoEqn Time = 0.00036 s +rhoEqn assamble = 0.000284 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001303 s +UEqn assamble = 0.000779 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000524 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001467 s +YEqn assamble = 0.000535 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.2e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000389 s +EEqn assamble = 0.000274 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 261.91 s ClockTime = 262 s +Courant Number mean: 0.00409655 max: 0.0227293 +Time = 0.001995 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21836 + Current mass in system = 1.17746e-09 + Linear momentum = (1.59565e-11 -5.27599e-09 0) + |Linear momentum| = 5.27601e-09 + Linear kinetic energy = 1.31638e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 442.465, 540.2 + Mass transfer phase change = 5.28682e-10 + D10, D32, Dmax (mu) = 52.4035, 74.8039, 181.881 + Liquid penetration 95% mass (m) = 0.0132033 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0170774, Final residual = 9.31813e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0227322, Final residual = 7.61212e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000659264, Final residual = 4.0647e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000168118, Final residual = 1.90677e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000260995, Final residual = 2.67147e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000260893, Final residual = 2.68214e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000561329, Final residual = 3.08931e-08, No Iterations 1 +min/max(T) = 806.895, 2729.7 +GAMG: Solving for p, Initial residual = 0.0473454, Final residual = 0.000401821, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.96836e-05, global = 2.86032e-05, cumulative = 0.0120721 +GAMG: Solving for p, Initial residual = 0.000387121, Final residual = 7.04575e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.85307e-05, global = 2.85288e-05, cumulative = 0.0121007 +smoothSolver: Solving for epsilon, Initial residual = 0.000609718, Final residual = 8.94491e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000650476, Final residual = 1.2102e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.111402 s +other Time = 0 s +rho Equations = 0.000181 s +U Equations = 0.001336 s +Y Equations = 0.00247452 s +E Equations = 0.000607 s +p Equations = 0.002572 s +calculate parcels = 184.207 s +chemistry correctThermo = 0.002858 s +turbulence correct = 0.001012 s +combustion correct(in Y) = 0.10015 s +percentage of chemistry = 89.9001 % +percentage of rho/U/Y/E = 4.12786 % +========Time details of each equation======= +rhoEqn Time = 0.000351 s +rhoEqn assamble = 0.000277 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001335 s +UEqn assamble = 0.0008 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000535 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001834 s +YEqn assamble = 0.000617 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000221 s +YEqn correct boundary = 0 s +EEqn Time = 0.000446 s +EEqn assamble = 0.000329 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 262.38 s ClockTime = 263 s +Courant Number mean: 0.00402286 max: 0.0223913 +Time = 0.0019975 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21836 + Current mass in system = 1.17499e-09 + Linear momentum = (1.58747e-11 -5.24345e-09 0) + |Linear momentum| = 5.24347e-09 + Linear kinetic energy = 1.30523e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 442.678, 540.2 + Mass transfer phase change = 5.3115e-10 + D10, D32, Dmax (mu) = 52.1392, 74.5905, 181.634 + Liquid penetration 95% mass (m) = 0.0132114 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.016591, Final residual = 8.66209e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0258368, Final residual = 8.67824e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000656132, Final residual = 4.06035e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000169805, Final residual = 1.94285e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000262866, Final residual = 2.70376e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000262775, Final residual = 2.71442e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000556559, Final residual = 3.07281e-08, No Iterations 1 +min/max(T) = 806.855, 2729.91 +GAMG: Solving for p, Initial residual = 0.0434718, Final residual = 0.000320324, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.94369e-05, global = 2.85313e-05, cumulative = 0.0121292 +GAMG: Solving for p, Initial residual = 0.000304529, Final residual = 3.49587e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.84499e-05, global = 2.84488e-05, cumulative = 0.0121576 +smoothSolver: Solving for epsilon, Initial residual = 0.00059156, Final residual = 8.60308e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000641127, Final residual = 1.17529e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102222 s +other Time = 0 s +rho Equations = 0.000181 s +U Equations = 0.001221 s +Y Equations = 0.00245236 s +E Equations = 0.000606 s +p Equations = 0.002406 s +calculate parcels = 184.563 s +chemistry correctThermo = 0.00285 s +turbulence correct = 0.001115 s +combustion correct(in Y) = 0.0911886 s +percentage of chemistry = 89.2065 % +percentage of rho/U/Y/E = 4.36341 % +========Time details of each equation======= +rhoEqn Time = 0.000366 s +rhoEqn assamble = 0.000265 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000101 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00122 s +UEqn assamble = 0.000785 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000435 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001895 s +YEqn assamble = 0.000665 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00024 s +YEqn correct boundary = 0 s +EEqn Time = 0.000445 s +EEqn assamble = 0.00033 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 262.84 s ClockTime = 263 s +Courant Number mean: 0.00394035 max: 0.02203 +Time = 0.002 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21836 + Current mass in system = 1.17254e-09 + Linear momentum = (1.58241e-11 -5.21185e-09 0) + |Linear momentum| = 5.21188e-09 + Linear kinetic energy = 1.29447e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 442.892, 540.2 + Mass transfer phase change = 5.33606e-10 + D10, D32, Dmax (mu) = 51.8828, 74.3815, 181.389 + Liquid penetration 95% mass (m) = 0.01322 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0175576, Final residual = 9.17339e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0289668, Final residual = 9.7797e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000653091, Final residual = 4.04781e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000174361, Final residual = 1.98968e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00026663, Final residual = 2.74963e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000266556, Final residual = 2.76067e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00055349, Final residual = 3.06254e-08, No Iterations 1 +min/max(T) = 806.817, 2730.17 +GAMG: Solving for p, Initial residual = 0.0402509, Final residual = 0.000282687, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.92379e-05, global = 2.84044e-05, cumulative = 0.0121861 +GAMG: Solving for p, Initial residual = 0.000270563, Final residual = 4.19855e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.83137e-05, global = 2.83125e-05, cumulative = 0.0122144 +smoothSolver: Solving for epsilon, Initial residual = 0.000575059, Final residual = 8.2437e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000632325, Final residual = 1.14132e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.075895 s +other Time = 0 s +rho Equations = 0.000169 s +U Equations = 0.001044 s +Y Equations = 0.00241544 s +E Equations = 0.000595 s +p Equations = 0.001949 s +calculate parcels = 184.92 s +chemistry correctThermo = 0.002013 s +turbulence correct = 0.000876 s +combustion correct(in Y) = 0.0666536 s +percentage of chemistry = 87.8234 % +percentage of rho/U/Y/E = 5.56485 % +========Time details of each equation======= +rhoEqn Time = 0.000294 s +rhoEqn assamble = 0.000233 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001043 s +UEqn assamble = 0.000617 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000426 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001674 s +YEqn assamble = 0.000621 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 7.3e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000468 s +EEqn assamble = 0.000356 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 263.54 s ClockTime = 264 s +Courant Number mean: 0.00385073 max: 0.0215811 +Time = 0.0020025 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21836 + Current mass in system = 1.17009e-09 + Linear momentum = (1.58098e-11 -5.18128e-09 0) + |Linear momentum| = 5.1813e-09 + Linear kinetic energy = 1.28412e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 443.106, 540.2 + Mass transfer phase change = 5.36048e-10 + D10, D32, Dmax (mu) = 51.6356, 74.1778, 181.145 + Liquid penetration 95% mass (m) = 0.0132277 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0196198, Final residual = 1.04182e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.03217, Final residual = 1.09079e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000651834, Final residual = 4.08125e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000181007, Final residual = 2.05004e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000273148, Final residual = 2.81019e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000273081, Final residual = 2.82159e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000553127, Final residual = 3.08863e-08, No Iterations 1 +min/max(T) = 806.781, 2730.43 +GAMG: Solving for p, Initial residual = 0.0374707, Final residual = 0.000243149, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.8986e-05, global = 2.82135e-05, cumulative = 0.0122426 +GAMG: Solving for p, Initial residual = 0.000232656, Final residual = 3.8518e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.81467e-05, global = 2.81456e-05, cumulative = 0.0122707 +smoothSolver: Solving for epsilon, Initial residual = 0.000562011, Final residual = 7.91582e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000625203, Final residual = 1.11287e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.108927 s +other Time = 0 s +rho Equations = 0.000176 s +U Equations = 0.000976 s +Y Equations = 0.00238804 s +E Equations = 0.000589 s +p Equations = 0.002239 s +calculate parcels = 185.279 s +chemistry correctThermo = 0.002873 s +turbulence correct = 0.001034 s +combustion correct(in Y) = 0.098476 s +percentage of chemistry = 90.4055 % +percentage of rho/U/Y/E = 3.79065 % +========Time details of each equation======= +rhoEqn Time = 0.000321 s +rhoEqn assamble = 0.000255 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000975 s +UEqn assamble = 0.000557 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000418 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001848 s +YEqn assamble = 0.000643 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000239 s +YEqn correct boundary = 0 s +EEqn Time = 0.000433 s +EEqn assamble = 0.000322 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 264.01 s ClockTime = 265 s +Courant Number mean: 0.00375528 max: 0.0211407 +Time = 0.002005 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21836 + Current mass in system = 1.16767e-09 + Linear momentum = (1.58329e-11 -5.15174e-09 0) + |Linear momentum| = 5.15177e-09 + Linear kinetic energy = 1.27418e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 443.32, 540.2 + Mass transfer phase change = 5.38474e-10 + D10, D32, Dmax (mu) = 51.3994, 73.9797, 180.903 + Liquid penetration 95% mass (m) = 0.0132349 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0220383, Final residual = 1.12186e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0354256, Final residual = 1.19779e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00065126, Final residual = 4.0938e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000188502, Final residual = 2.10529e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000279613, Final residual = 2.86136e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00027955, Final residual = 2.87301e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000551564, Final residual = 3.09113e-08, No Iterations 1 +min/max(T) = 806.747, 2730.66 +GAMG: Solving for p, Initial residual = 0.0349121, Final residual = 0.000201084, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.87142e-05, global = 2.80193e-05, cumulative = 0.0122987 +GAMG: Solving for p, Initial residual = 0.000193595, Final residual = 1.89638e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.79616e-05, global = 2.79608e-05, cumulative = 0.0123267 +smoothSolver: Solving for epsilon, Initial residual = 0.000549889, Final residual = 7.6236e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000618995, Final residual = 1.08756e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.110786 s +other Time = 0 s +rho Equations = 0.000181 s +U Equations = 0.001183 s +Y Equations = 0.00258814 s +E Equations = 0.00061 s +p Equations = 0.002329 s +calculate parcels = 185.619 s +chemistry correctThermo = 0.002888 s +turbulence correct = 0.001073 s +combustion correct(in Y) = 0.0997379 s +percentage of chemistry = 90.0275 % +percentage of rho/U/Y/E = 4.11798 % +========Time details of each equation======= +rhoEqn Time = 0.000324 s +rhoEqn assamble = 0.000255 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001183 s +UEqn assamble = 0.000685 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000498 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001938 s +YEqn assamble = 0.000674 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000213 s +YEqn correct boundary = 0 s +EEqn Time = 0.000452 s +EEqn assamble = 0.000341 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 264.46 s ClockTime = 265 s +Courant Number mean: 0.00365343 max: 0.0207035 +Time = 0.0020075 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21836 + Current mass in system = 1.16526e-09 + Linear momentum = (1.58872e-11 -5.12321e-09 0) + |Linear momentum| = 5.12324e-09 + Linear kinetic energy = 1.26463e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 443.534, 540.2 + Mass transfer phase change = 5.40883e-10 + D10, D32, Dmax (mu) = 51.1737, 73.7869, 180.662 + Liquid penetration 95% mass (m) = 0.0132426 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0231796, Final residual = 1.18866e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0387324, Final residual = 1.30007e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000649658, Final residual = 4.09238e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000196765, Final residual = 2.16175e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00028569, Final residual = 2.90703e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000285618, Final residual = 2.91877e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000549851, Final residual = 3.09623e-08, No Iterations 1 +min/max(T) = 806.714, 2730.88 +GAMG: Solving for p, Initial residual = 0.0325849, Final residual = 0.000179737, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.84762e-05, global = 2.77986e-05, cumulative = 0.0123545 +GAMG: Solving for p, Initial residual = 0.000173539, Final residual = 2.07201e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.77669e-05, global = 2.77661e-05, cumulative = 0.0123823 +smoothSolver: Solving for epsilon, Initial residual = 0.000537865, Final residual = 7.36124e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000614362, Final residual = 1.06401e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.111443 s +other Time = 0 s +rho Equations = 0.000189 s +U Equations = 0.001232 s +Y Equations = 0.00243161 s +E Equations = 0.000604 s +p Equations = 0.002263 s +calculate parcels = 185.961 s +chemistry correctThermo = 0.002878 s +turbulence correct = 0.001103 s +combustion correct(in Y) = 0.1005 s +percentage of chemistry = 90.181 % +percentage of rho/U/Y/E = 3.999 % +========Time details of each equation======= +rhoEqn Time = 0.000329 s +rhoEqn assamble = 0.00026 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001231 s +UEqn assamble = 0.000699 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000532 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001755 s +YEqn assamble = 0.000628 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000179 s +YEqn correct boundary = 0 s +EEqn Time = 0.000448 s +EEqn assamble = 0.000326 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000122 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 264.91 s ClockTime = 265 s +Courant Number mean: 0.00354524 max: 0.020382 +Time = 0.00201 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21836 + Current mass in system = 1.16287e-09 + Linear momentum = (1.59538e-11 -5.09569e-09 0) + |Linear momentum| = 5.09571e-09 + Linear kinetic energy = 1.25546e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 443.748, 540.2 + Mass transfer phase change = 5.43274e-10 + D10, D32, Dmax (mu) = 50.9578, 73.5997, 180.422 + Liquid penetration 95% mass (m) = 0.0132508 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0231758, Final residual = 1.21042e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0421636, Final residual = 1.39976e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000647814, Final residual = 4.09363e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000204623, Final residual = 2.20839e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000291075, Final residual = 2.93796e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000291007, Final residual = 2.94967e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000548345, Final residual = 3.1094e-08, No Iterations 1 +min/max(T) = 806.683, 2731.1 +GAMG: Solving for p, Initial residual = 0.0304186, Final residual = 0.000164041, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.82226e-05, global = 2.75702e-05, cumulative = 0.0124098 +GAMG: Solving for p, Initial residual = 0.000158424, Final residual = 2.27174e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.75533e-05, global = 2.75524e-05, cumulative = 0.0124374 +smoothSolver: Solving for epsilon, Initial residual = 0.0005264, Final residual = 7.07011e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000610029, Final residual = 1.04067e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.093593 s +other Time = 0 s +rho Equations = 0.000171 s +U Equations = 0.001316 s +Y Equations = 0.00206408 s +E Equations = 0.000486 s +p Equations = 0.001776 s +calculate parcels = 186.298 s +chemistry correctThermo = 0.00207 s +turbulence correct = 0.000789 s +combustion correct(in Y) = 0.0847269 s +percentage of chemistry = 90.527 % +percentage of rho/U/Y/E = 4.31344 % +========Time details of each equation======= +rhoEqn Time = 0.000288 s +rhoEqn assamble = 0.000228 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001315 s +UEqn assamble = 0.000806 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000509 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001412 s +YEqn assamble = 0.000509 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.1e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000365 s +EEqn assamble = 0.000271 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 265.34 s ClockTime = 266 s +Courant Number mean: 0.00343028 max: 0.0200493 +Time = 0.0020125 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21836 + Current mass in system = 1.1605e-09 + Linear momentum = (1.60263e-11 -5.06922e-09 0) + |Linear momentum| = 5.06924e-09 + Linear kinetic energy = 1.24669e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 443.961, 540.2 + Mass transfer phase change = 5.45644e-10 + D10, D32, Dmax (mu) = 50.7529, 73.4186, 180.361 + Liquid penetration 95% mass (m) = 0.0132578 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0223626, Final residual = 1.20065e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0457576, Final residual = 1.49952e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000646093, Final residual = 4.0886e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000212602, Final residual = 2.239e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000296715, Final residual = 2.94405e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000296651, Final residual = 2.95571e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000546276, Final residual = 3.1128e-08, No Iterations 1 +min/max(T) = 806.654, 2731.35 +GAMG: Solving for p, Initial residual = 0.0283221, Final residual = 0.00014136, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.79203e-05, global = 2.7324e-05, cumulative = 0.0124647 +GAMG: Solving for p, Initial residual = 0.000137554, Final residual = 1.65578e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.73116e-05, global = 2.73109e-05, cumulative = 0.012492 +smoothSolver: Solving for epsilon, Initial residual = 0.000514654, Final residual = 6.79294e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000606723, Final residual = 1.01945e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.075797 s +other Time = 1e-06 s +rho Equations = 0.000176 s +U Equations = 0.001053 s +Y Equations = 0.00233398 s +E Equations = 0.000544 s +p Equations = 0.001977 s +calculate parcels = 186.576 s +chemistry correctThermo = 0.002033 s +turbulence correct = 0.000939 s +combustion correct(in Y) = 0.066545 s +percentage of chemistry = 87.7937 % +percentage of rho/U/Y/E = 5.4184 % +========Time details of each equation======= +rhoEqn Time = 0.000316 s +rhoEqn assamble = 0.00024 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001053 s +UEqn assamble = 0.000637 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000416 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001738 s +YEqn assamble = 0.000557 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000138 s +YEqn correct boundary = 0 s +EEqn Time = 0.000415 s +EEqn assamble = 0.000316 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 265.7 s ClockTime = 266 s +Courant Number mean: 0.00330842 max: 0.0195494 +Time = 0.002015 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21836 + Current mass in system = 1.15815e-09 + Linear momentum = (1.60992e-11 -5.04383e-09 0) + |Linear momentum| = 5.04386e-09 + Linear kinetic energy = 1.23833e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 444.174, 540.2 + Mass transfer phase change = 5.47989e-10 + D10, D32, Dmax (mu) = 50.5586, 73.2439, 180.662 + Liquid penetration 95% mass (m) = 0.0132655 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0215619, Final residual = 1.16174e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0495373, Final residual = 1.5997e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000644122, Final residual = 4.08826e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00022057, Final residual = 2.25867e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000302457, Final residual = 2.94283e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000302398, Final residual = 2.95436e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000544709, Final residual = 3.12786e-08, No Iterations 1 +min/max(T) = 806.626, 2731.64 +GAMG: Solving for p, Initial residual = 0.0263792, Final residual = 0.000119109, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.75823e-05, global = 2.70463e-05, cumulative = 0.0125191 +GAMG: Solving for p, Initial residual = 0.000116557, Final residual = 8.75683e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.70416e-05, global = 2.70375e-05, cumulative = 0.0125461 +smoothSolver: Solving for epsilon, Initial residual = 0.000505272, Final residual = 6.53596e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000605114, Final residual = 1.00171e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.114378 s +other Time = 0 s +rho Equations = 0.000191 s +U Equations = 0.001278 s +Y Equations = 0.00243173 s +E Equations = 0.000643 s +p Equations = 0.002035 s +calculate parcels = 186.837 s +chemistry correctThermo = 0.002896 s +turbulence correct = 0.001031 s +combustion correct(in Y) = 0.103641 s +percentage of chemistry = 90.6129 % +percentage of rho/U/Y/E = 3.97256 % +========Time details of each equation======= +rhoEqn Time = 0.000354 s +rhoEqn assamble = 0.000276 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001277 s +UEqn assamble = 0.000782 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000495 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001802 s +YEqn assamble = 0.000632 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000196 s +YEqn correct boundary = 0 s +EEqn Time = 0.000485 s +EEqn assamble = 0.000367 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 266.07 s ClockTime = 267 s +Courant Number mean: 0.00318015 max: 0.0190858 +Time = 0.0020175 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21836 + Current mass in system = 1.15583e-09 + Linear momentum = (1.61734e-11 -5.01955e-09 0) + |Linear momentum| = 5.01958e-09 + Linear kinetic energy = 1.23037e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 444.385, 540.2 + Mass transfer phase change = 5.50309e-10 + D10, D32, Dmax (mu) = 50.3752, 73.0757, 180.949 + Liquid penetration 95% mass (m) = 0.0132736 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0213886, Final residual = 1.12071e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0535363, Final residual = 1.70039e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000642053, Final residual = 4.07331e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000229159, Final residual = 2.27147e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000308774, Final residual = 2.94189e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000308716, Final residual = 2.95327e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000543571, Final residual = 3.13472e-08, No Iterations 1 +min/max(T) = 806.601, 2731.96 +GAMG: Solving for p, Initial residual = 0.0245672, Final residual = 0.000105871, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.723e-05, global = 2.67338e-05, cumulative = 0.0125728 +GAMG: Solving for p, Initial residual = 0.000103173, Final residual = 6.64133e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.67392e-05, global = 2.67361e-05, cumulative = 0.0125996 +smoothSolver: Solving for epsilon, Initial residual = 0.000500018, Final residual = 6.28626e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000606369, Final residual = 9.8566e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.107221 s +other Time = 1e-06 s +rho Equations = 0.00018 s +U Equations = 0.001321 s +Y Equations = 0.0023239 s +E Equations = 0.000486 s +p Equations = 0.001669 s +calculate parcels = 187.188 s +chemistry correctThermo = 0.002013 s +turbulence correct = 0.000809 s +combustion correct(in Y) = 0.0982201 s +percentage of chemistry = 91.6053 % +percentage of rho/U/Y/E = 4.02057 % +========Time details of each equation======= +rhoEqn Time = 0.0003 s +rhoEqn assamble = 0.000235 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00132 s +UEqn assamble = 0.000796 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000524 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001674 s +YEqn assamble = 0.000607 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000158 s +YEqn correct boundary = 0 s +EEqn Time = 0.000363 s +EEqn assamble = 0.000272 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 266.53 s ClockTime = 267 s +Courant Number mean: 0.00304591 max: 0.0187839 +Time = 0.00202 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21836 + Current mass in system = 1.15354e-09 + Linear momentum = (1.62458e-11 -4.99639e-09 0) + |Linear momentum| = 4.99642e-09 + Linear kinetic energy = 1.22282e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 444.596, 540.2 + Mass transfer phase change = 5.526e-10 + D10, D32, Dmax (mu) = 50.2025, 72.9145, 181.054 + Liquid penetration 95% mass (m) = 0.0132811 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0206332, Final residual = 1.0502e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0577367, Final residual = 1.79924e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000639813, Final residual = 4.0457e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000237447, Final residual = 2.27051e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000315191, Final residual = 2.9329e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00031513, Final residual = 2.94414e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000542268, Final residual = 3.13552e-08, No Iterations 1 +min/max(T) = 806.577, 2732.31 +GAMG: Solving for p, Initial residual = 0.0228722, Final residual = 9.76105e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.68681e-05, global = 2.63995e-05, cumulative = 0.012626 +GAMG: Solving for p, Initial residual = 9.43251e-05, Final residual = 6.46877e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.64095e-05, global = 2.64064e-05, cumulative = 0.0126524 +smoothSolver: Solving for epsilon, Initial residual = 0.000502557, Final residual = 6.08445e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000609039, Final residual = 9.74756e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.10442 s +other Time = 0 s +rho Equations = 0.000224 s +U Equations = 0.001642 s +Y Equations = 0.00265832 s +E Equations = 0.000631 s +p Equations = 0.002207 s +calculate parcels = 187.559 s +chemistry correctThermo = 0.002902 s +turbulence correct = 0.001092 s +combustion correct(in Y) = 0.0928127 s +percentage of chemistry = 88.884 % +percentage of rho/U/Y/E = 4.9371 % +========Time details of each equation======= +rhoEqn Time = 0.000376 s +rhoEqn assamble = 0.00029 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00164 s +UEqn assamble = 0.000886 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000754 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001594 s +YEqn assamble = 0.000643 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -2e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000458 s +EEqn assamble = 0.000342 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 267.01 s ClockTime = 268 s +Courant Number mean: 0.0029063 max: 0.0184291 +Time = 0.0020225 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21836 + Current mass in system = 1.15128e-09 + Linear momentum = (1.632e-11 -4.97434e-09 0) + |Linear momentum| = 4.97436e-09 + Linear kinetic energy = 1.21565e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 444.806, 540.2 + Mass transfer phase change = 5.5486e-10 + D10, D32, Dmax (mu) = 50.0415, 72.7607, 180.837 + Liquid penetration 95% mass (m) = 0.0132882 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0197808, Final residual = 9.78309e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0621363, Final residual = 1.89671e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000636384, Final residual = 4.00966e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000245812, Final residual = 2.26607e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000321064, Final residual = 2.91941e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000320998, Final residual = 2.9304e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000540435, Final residual = 3.12518e-08, No Iterations 1 +min/max(T) = 806.555, 2732.68 +GAMG: Solving for p, Initial residual = 0.0213239, Final residual = 9.14469e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.64996e-05, global = 2.60278e-05, cumulative = 0.0126784 +GAMG: Solving for p, Initial residual = 8.92183e-05, Final residual = 6.61681e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.6052e-05, global = 2.60486e-05, cumulative = 0.0127045 +smoothSolver: Solving for epsilon, Initial residual = 0.000504047, Final residual = 5.95992e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000611802, Final residual = 9.66982e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097057 s +other Time = 0 s +rho Equations = 0.000153 s +U Equations = 0.000981 s +Y Equations = 0.00238576 s +E Equations = 0.000625 s +p Equations = 0.002042 s +calculate parcels = 187.889 s +chemistry correctThermo = 0.002871 s +turbulence correct = 0.000973 s +combustion correct(in Y) = 0.0868542 s +percentage of chemistry = 89.4879 % +percentage of rho/U/Y/E = 4.27044 % +========Time details of each equation======= +rhoEqn Time = 0.000299 s +rhoEqn assamble = 0.000236 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000981 s +UEqn assamble = 0.000577 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000404 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001842 s +YEqn assamble = 0.000627 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000225 s +YEqn correct boundary = 0 s +EEqn Time = 0.000452 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 267.43 s ClockTime = 268 s +Courant Number mean: 0.0027616 max: 0.0179949 +Time = 0.002025 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21835 + Current mass in system = 1.14906e-09 + Linear momentum = (1.63979e-11 -4.95339e-09 0) + |Linear momentum| = 4.95342e-09 + Linear kinetic energy = 1.20888e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 445.016, 540.2 + Mass transfer phase change = 5.57087e-10 + D10, D32, Dmax (mu) = 49.9249, 72.6148, 180.623 + Liquid penetration 95% mass (m) = 0.0132951 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0189024, Final residual = 9.09701e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.066674, Final residual = 1.9901e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000635161, Final residual = 3.9806e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000253999, Final residual = 2.2507e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000326361, Final residual = 2.90199e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000326298, Final residual = 2.91272e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000540156, Final residual = 3.13948e-08, No Iterations 1 +min/max(T) = 806.536, 2733.08 +GAMG: Solving for p, Initial residual = 0.0198766, Final residual = 9.02663e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.61111e-05, global = 2.56333e-05, cumulative = 0.0127301 +GAMG: Solving for p, Initial residual = 8.78477e-05, Final residual = 6.77799e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.56741e-05, global = 2.56705e-05, cumulative = 0.0127558 +smoothSolver: Solving for epsilon, Initial residual = 0.000507059, Final residual = 5.89602e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000616061, Final residual = 9.61218e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100969 s +other Time = 0 s +rho Equations = 0.000184 s +U Equations = 0.001165 s +Y Equations = 0.00417282 s +E Equations = 0.000991 s +p Equations = 0.001789 s +calculate parcels = 188.259 s +chemistry correctThermo = 0.002172 s +turbulence correct = 0.000913 s +combustion correct(in Y) = 0.0893732 s +percentage of chemistry = 88.5155 % +percentage of rho/U/Y/E = 6.45031 % +========Time details of each equation======= +rhoEqn Time = 0.0003 s +rhoEqn assamble = 0.000237 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001163 s +UEqn assamble = 0.000696 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000467 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.0036 s +YEqn assamble = 0.001145 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000718 s +YEqn correct boundary = 0 s +EEqn Time = 0.000745 s +EEqn assamble = 0.000532 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000213 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 267.9 s ClockTime = 268 s +Courant Number mean: 0.00261222 max: 0.0174228 +Time = 0.0020275 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21835 + Current mass in system = 1.14687e-09 + Linear momentum = (1.64734e-11 -4.93359e-09 0) + |Linear momentum| = 4.93362e-09 + Linear kinetic energy = 1.2025e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 445.225, 540.2 + Mass transfer phase change = 5.59276e-10 + D10, D32, Dmax (mu) = 49.7842, 72.4763, 180.412 + Liquid penetration 95% mass (m) = 0.0133029 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0179786, Final residual = 8.38361e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0713963, Final residual = 2.07996e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000632904, Final residual = 3.94478e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000261538, Final residual = 2.20955e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000331347, Final residual = 2.8593e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000331288, Final residual = 2.86984e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000538387, Final residual = 3.13129e-08, No Iterations 1 +min/max(T) = 806.518, 2733.46 +GAMG: Solving for p, Initial residual = 0.0184777, Final residual = 8.58811e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.5665e-05, global = 2.5185e-05, cumulative = 0.012781 +GAMG: Solving for p, Initial residual = 8.31843e-05, Final residual = 6.41003e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.52318e-05, global = 2.52281e-05, cumulative = 0.0128062 +smoothSolver: Solving for epsilon, Initial residual = 0.000516423, Final residual = 5.85966e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000623096, Final residual = 9.591e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.07682 s +other Time = 0 s +rho Equations = 0.000176 s +U Equations = 0.001024 s +Y Equations = 0.00219466 s +E Equations = 0.000542 s +p Equations = 0.001755 s +calculate parcels = 188.538 s +chemistry correctThermo = 0.001958 s +turbulence correct = 0.00087 s +combustion correct(in Y) = 0.0681133 s +percentage of chemistry = 88.6662 % +percentage of rho/U/Y/E = 5.12452 % +========Time details of each equation======= +rhoEqn Time = 0.0003 s +rhoEqn assamble = 0.000238 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001024 s +UEqn assamble = 0.000604 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00042 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001623 s +YEqn assamble = 0.000566 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000138 s +YEqn correct boundary = 0 s +EEqn Time = 0.000417 s +EEqn assamble = 0.00031 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000107 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 268.26 s ClockTime = 269 s +Courant Number mean: 0.00245997 max: 0.0166909 +Time = 0.00203 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21835 + Current mass in system = 1.14472e-09 + Linear momentum = (1.65507e-11 -4.91494e-09 0) + |Linear momentum| = 4.91497e-09 + Linear kinetic energy = 1.19651e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 445.433, 540.2 + Mass transfer phase change = 5.61424e-10 + D10, D32, Dmax (mu) = 49.6534, 72.346, 180.203 + Liquid penetration 95% mass (m) = 0.0133098 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0169478, Final residual = 7.72373e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.076225, Final residual = 2.16463e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000630434, Final residual = 3.91948e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000269127, Final residual = 2.18466e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000335385, Final residual = 2.82638e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000335331, Final residual = 2.83676e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00053521, Final residual = 3.13616e-08, No Iterations 1 +min/max(T) = 806.503, 2733.81 +GAMG: Solving for p, Initial residual = 0.0172297, Final residual = 8.70979e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.52289e-05, global = 2.4711e-05, cumulative = 0.0128309 +GAMG: Solving for p, Initial residual = 8.45208e-05, Final residual = 6.21365e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.47606e-05, global = 2.47567e-05, cumulative = 0.0128556 +smoothSolver: Solving for epsilon, Initial residual = 0.000531294, Final residual = 5.88618e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00063046, Final residual = 9.57422e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.105951 s +other Time = 0 s +rho Equations = 0.00019 s +U Equations = 0.001301 s +Y Equations = 0.00276506 s +E Equations = 0.000767 s +p Equations = 0.00283 s +calculate parcels = 188.875 s +chemistry correctThermo = 0.003119 s +turbulence correct = 0.001258 s +combustion correct(in Y) = 0.0934859 s +percentage of chemistry = 88.2351 % +percentage of rho/U/Y/E = 4.74093 % +========Time details of each equation======= +rhoEqn Time = 0.000407 s +rhoEqn assamble = 0.000311 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001301 s +UEqn assamble = 0.000768 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000533 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002032 s +YEqn assamble = 0.000727 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000198 s +YEqn correct boundary = 0 s +EEqn Time = 0.000564 s +EEqn assamble = 0.000418 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000146 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 268.7 s ClockTime = 269 s +Courant Number mean: 0.00230416 max: 0.015838 +Time = 0.0020325 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21835 + Current mass in system = 1.14262e-09 + Linear momentum = (1.66334e-11 -4.89748e-09 0) + |Linear momentum| = 4.8975e-09 + Linear kinetic energy = 1.19092e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 445.641, 540.2 + Mass transfer phase change = 5.63527e-10 + D10, D32, Dmax (mu) = 49.5315, 72.2247, 179.997 + Liquid penetration 95% mass (m) = 0.0133168 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0163047, Final residual = 7.1636e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0812503, Final residual = 2.24779e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000630408, Final residual = 3.89748e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000276578, Final residual = 2.14517e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000338548, Final residual = 2.77905e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000338496, Final residual = 2.78929e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000532702, Final residual = 3.14341e-08, No Iterations 1 +min/max(T) = 806.489, 2734.12 +GAMG: Solving for p, Initial residual = 0.016016, Final residual = 8.07978e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.468e-05, global = 2.4178e-05, cumulative = 0.0128798 +GAMG: Solving for p, Initial residual = 7.83615e-05, Final residual = 5.72267e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.42338e-05, global = 2.42303e-05, cumulative = 0.0129041 +smoothSolver: Solving for epsilon, Initial residual = 0.000553108, Final residual = 6.00024e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000639919, Final residual = 9.58005e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.106649 s +other Time = 1e-06 s +rho Equations = 0.000203 s +U Equations = 0.001365 s +Y Equations = 0.00216067 s +E Equations = 0.000481 s +p Equations = 0.001685 s +calculate parcels = 189.271 s +chemistry correctThermo = 0.00202 s +turbulence correct = 0.000807 s +combustion correct(in Y) = 0.0976773 s +percentage of chemistry = 91.5877 % +percentage of rho/U/Y/E = 3.94722 % +========Time details of each equation======= +rhoEqn Time = 0.000318 s +rhoEqn assamble = 0.000251 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001364 s +UEqn assamble = 0.000774 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00059 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001408 s +YEqn assamble = 0.000546 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 3.8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000364 s +EEqn assamble = 0.000273 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 269.21 s ClockTime = 270 s +Courant Number mean: 0.00214537 max: 0.0153703 +Time = 0.002035 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21835 + Current mass in system = 1.14056e-09 + Linear momentum = (1.67221e-11 -4.88121e-09 0) + |Linear momentum| = 4.88124e-09 + Linear kinetic energy = 1.18573e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 445.848, 540.2 + Mass transfer phase change = 5.65578e-10 + D10, D32, Dmax (mu) = 49.4191, 72.113, 179.793 + Liquid penetration 95% mass (m) = 0.0133237 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0160795, Final residual = 6.80686e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0864303, Final residual = 2.32646e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000631542, Final residual = 3.86813e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000284268, Final residual = 2.10012e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000341559, Final residual = 2.72058e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000341514, Final residual = 2.73075e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000531447, Final residual = 3.14808e-08, No Iterations 1 +min/max(T) = 806.478, 2734.41 +GAMG: Solving for p, Initial residual = 0.0149005, Final residual = 8.28198e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.41287e-05, global = 2.35877e-05, cumulative = 0.0129276 +GAMG: Solving for p, Initial residual = 8.04788e-05, Final residual = 6.13411e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.36459e-05, global = 2.36422e-05, cumulative = 0.0129513 +smoothSolver: Solving for epsilon, Initial residual = 0.000580085, Final residual = 6.17575e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000651687, Final residual = 9.64462e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092541 s +other Time = 0 s +rho Equations = 0.000152 s +U Equations = 0.00116 s +Y Equations = 0.00260022 s +E Equations = 0.000616 s +p Equations = 0.002069 s +calculate parcels = 189.62 s +chemistry correctThermo = 0.002894 s +turbulence correct = 0.001069 s +combustion correct(in Y) = 0.0818008 s +percentage of chemistry = 88.3941 % +percentage of rho/U/Y/E = 4.8932 % +========Time details of each equation======= +rhoEqn Time = 0.000296 s +rhoEqn assamble = 0.000234 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001159 s +UEqn assamble = 0.000736 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000423 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00204 s +YEqn assamble = 0.000702 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000259 s +YEqn correct boundary = 0 s +EEqn Time = 0.000446 s +EEqn assamble = 0.000333 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 269.65 s ClockTime = 270 s +Courant Number mean: 0.00198591 max: 0.0149211 +Time = 0.0020375 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21835 + Current mass in system = 1.13857e-09 + Linear momentum = (1.68145e-11 -4.86611e-09 0) + |Linear momentum| = 4.86614e-09 + Linear kinetic energy = 1.18091e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 446.055, 540.2 + Mass transfer phase change = 5.67574e-10 + D10, D32, Dmax (mu) = 49.3157, 72.0111, 179.591 + Liquid penetration 95% mass (m) = 0.0133314 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0160285, Final residual = 6.49116e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0917742, Final residual = 2.40224e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000631648, Final residual = 3.89109e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000291245, Final residual = 2.05429e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000343784, Final residual = 2.65437e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00034374, Final residual = 2.66437e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000530583, Final residual = 3.15771e-08, No Iterations 1 +min/max(T) = 806.469, 2734.64 +GAMG: Solving for p, Initial residual = 0.0139105, Final residual = 0.000100451, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.35969e-05, global = 2.29295e-05, cumulative = 0.0129742 +GAMG: Solving for p, Initial residual = 9.74311e-05, Final residual = 8.15466e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.30107e-05, global = 2.30053e-05, cumulative = 0.0129972 +smoothSolver: Solving for epsilon, Initial residual = 0.000610307, Final residual = 6.36689e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000666262, Final residual = 9.7352e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102532 s +other Time = 1e-06 s +rho Equations = 0.000158 s +U Equations = 0.001082 s +Y Equations = 0.00253227 s +E Equations = 0.000626 s +p Equations = 0.002025 s +calculate parcels = 189.959 s +chemistry correctThermo = 0.002872 s +turbulence correct = 0.000965 s +combustion correct(in Y) = 0.0920467 s +percentage of chemistry = 89.7737 % +percentage of rho/U/Y/E = 4.28966 % +========Time details of each equation======= +rhoEqn Time = 0.000299 s +rhoEqn assamble = 0.000236 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001081 s +UEqn assamble = 0.000664 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000417 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001626 s +YEqn assamble = 0.000637 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 4.2e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000458 s +EEqn assamble = 0.000342 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 270.09 s ClockTime = 271 s +Courant Number mean: 0.00182757 max: 0.0144484 +Time = 0.00204 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21835 + Current mass in system = 1.13663e-09 + Linear momentum = (1.6905e-11 -4.85213e-09 0) + |Linear momentum| = 4.85216e-09 + Linear kinetic energy = 1.17645e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 446.263, 540.2 + Mass transfer phase change = 5.6951e-10 + D10, D32, Dmax (mu) = 49.2211, 71.9192, 179.392 + Liquid penetration 95% mass (m) = 0.0133387 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0166322, Final residual = 6.43531e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0972285, Final residual = 2.47424e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00062824, Final residual = 3.90985e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000297554, Final residual = 2.01102e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00034563, Final residual = 2.59512e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000345582, Final residual = 2.60471e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000526947, Final residual = 3.14418e-08, No Iterations 1 +min/max(T) = 806.462, 2735.1 +GAMG: Solving for p, Initial residual = 0.0128753, Final residual = 9.89068e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.29459e-05, global = 2.22405e-05, cumulative = 0.0130195 +GAMG: Solving for p, Initial residual = 9.57095e-05, Final residual = 1.90648e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.23098e-05, global = 2.23085e-05, cumulative = 0.0130418 +smoothSolver: Solving for epsilon, Initial residual = 0.000637824, Final residual = 6.60268e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000683859, Final residual = 9.90059e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.07962 s +other Time = 1e-06 s +rho Equations = 0.000217 s +U Equations = 0.001192 s +Y Equations = 0.00234674 s +E Equations = 0.000568 s +p Equations = 0.001911 s +calculate parcels = 190.301 s +chemistry correctThermo = 0.002089 s +turbulence correct = 0.000878 s +combustion correct(in Y) = 0.0700273 s +percentage of chemistry = 87.9519 % +percentage of rho/U/Y/E = 5.43046 % +========Time details of each equation======= +rhoEqn Time = 0.000343 s +rhoEqn assamble = 0.00026 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00119 s +UEqn assamble = 0.000764 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000426 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001767 s +YEqn assamble = 0.000572 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000156 s +YEqn correct boundary = 0 s +EEqn Time = 0.00044 s +EEqn assamble = 0.000283 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000157 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 270.51 s ClockTime = 271 s +Courant Number mean: 0.00167521 max: 0.0139762 +Time = 0.0020425 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21835 + Current mass in system = 1.13476e-09 + Linear momentum = (1.69859e-11 -4.83914e-09 0) + |Linear momentum| = 4.83917e-09 + Linear kinetic energy = 1.17232e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 446.47, 540.2 + Mass transfer phase change = 5.71385e-10 + D10, D32, Dmax (mu) = 49.1342, 71.8369, 179.196 + Liquid penetration 95% mass (m) = 0.0133457 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0175684, Final residual = 6.61856e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.102673, Final residual = 2.54475e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000625654, Final residual = 4.0206e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000304633, Final residual = 2.01397e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00034874, Final residual = 2.58952e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000348693, Final residual = 2.59888e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000523494, Final residual = 3.16125e-08, No Iterations 1 +min/max(T) = 806.457, 2735.86 +GAMG: Solving for p, Initial residual = 0.0120168, Final residual = 9.92816e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.22426e-05, global = 2.15364e-05, cumulative = 0.0130633 +GAMG: Solving for p, Initial residual = 9.63929e-05, Final residual = 7.91414e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.16203e-05, global = 2.16148e-05, cumulative = 0.0130849 +smoothSolver: Solving for epsilon, Initial residual = 0.000669519, Final residual = 6.91278e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000701757, Final residual = 1.01055e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.112552 s +other Time = 0 s +rho Equations = 0.000175 s +U Equations = 0.001314 s +Y Equations = 0.00256811 s +E Equations = 0.000618 s +p Equations = 0.003654 s +calculate parcels = 190.57 s +chemistry correctThermo = 0.003897 s +turbulence correct = 0.001796 s +combustion correct(in Y) = 0.0982929 s +percentage of chemistry = 87.3311 % +percentage of rho/U/Y/E = 4.15373 % +========Time details of each equation======= +rhoEqn Time = 0.000475 s +rhoEqn assamble = 0.000358 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000117 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001312 s +UEqn assamble = 0.000808 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000504 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00193 s +YEqn assamble = 0.000665 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000255 s +YEqn correct boundary = 0 s +EEqn Time = 0.00046 s +EEqn assamble = 0.000343 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 270.89 s ClockTime = 271 s +Courant Number mean: 0.00153189 max: 0.0135182 +Time = 0.002045 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21834 + Current mass in system = 1.13294e-09 + Linear momentum = (1.70468e-11 -4.827e-09 0) + |Linear momentum| = 4.82703e-09 + Linear kinetic energy = 1.16845e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 446.678, 540.2 + Mass transfer phase change = 5.73205e-10 + D10, D32, Dmax (mu) = 49.0866, 71.7641, 179.055 + Liquid penetration 95% mass (m) = 0.0133529 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0191603, Final residual = 7.37646e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.107872, Final residual = 2.6094e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000624554, Final residual = 4.0738e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000312483, Final residual = 2.03491e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000353776, Final residual = 2.61461e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000353731, Final residual = 2.62381e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00051973, Final residual = 3.17612e-08, No Iterations 1 +min/max(T) = 806.453, 2736.65 +GAMG: Solving for p, Initial residual = 0.0111055, Final residual = 9.69427e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.16082e-05, global = 2.08916e-05, cumulative = 0.0131058 +GAMG: Solving for p, Initial residual = 9.3807e-05, Final residual = 6.81614e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.09837e-05, global = 2.0979e-05, cumulative = 0.0131268 +smoothSolver: Solving for epsilon, Initial residual = 0.000699165, Final residual = 7.18665e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000717382, Final residual = 1.03005e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095084 s +other Time = 0 s +rho Equations = 0.000192 s +U Equations = 0.001277 s +Y Equations = 0.00260892 s +E Equations = 0.000649 s +p Equations = 0.002114 s +calculate parcels = 190.924 s +chemistry correctThermo = 0.00297 s +turbulence correct = 0.001082 s +combustion correct(in Y) = 0.0839801 s +percentage of chemistry = 88.322 % +percentage of rho/U/Y/E = 4.97131 % +========Time details of each equation======= +rhoEqn Time = 0.000339 s +rhoEqn assamble = 0.000264 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001276 s +UEqn assamble = 0.000761 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000515 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002099 s +YEqn assamble = 0.000778 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000196 s +YEqn correct boundary = 0 s +EEqn Time = 0.000474 s +EEqn assamble = 0.000362 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 271.34 s ClockTime = 272 s +Courant Number mean: 0.00141148 max: 0.0134663 +Time = 0.0020475 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21831 + Current mass in system = 1.13116e-09 + Linear momentum = (1.70916e-11 -4.81551e-09 0) + |Linear momentum| = 4.81554e-09 + Linear kinetic energy = 1.1648e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 446.886, 540.2 + Mass transfer phase change = 5.74986e-10 + D10, D32, Dmax (mu) = 49.0991, 71.7008, 178.938 + Liquid penetration 95% mass (m) = 0.0133608 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0207197, Final residual = 8.31045e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.112489, Final residual = 2.66805e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000627295, Final residual = 4.16593e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00032108, Final residual = 2.07039e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000360432, Final residual = 2.66084e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0003604, Final residual = 2.67001e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000517514, Final residual = 3.22566e-08, No Iterations 1 +min/max(T) = 806.45, 2737.45 +GAMG: Solving for p, Initial residual = 0.0103051, Final residual = 9.25817e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.11006e-05, global = 2.04306e-05, cumulative = 0.0131472 +GAMG: Solving for p, Initial residual = 8.86668e-05, Final residual = 6.51459e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.05303e-05, global = 2.05265e-05, cumulative = 0.0131677 +smoothSolver: Solving for epsilon, Initial residual = 0.000724443, Final residual = 7.45246e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000730405, Final residual = 1.05087e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.088197 s +other Time = 0 s +rho Equations = 0.000239 s +U Equations = 0.001396 s +Y Equations = 0.00252967 s +E Equations = 0.000631 s +p Equations = 0.002202 s +calculate parcels = 191.251 s +chemistry correctThermo = 0.002866 s +turbulence correct = 0.001094 s +combustion correct(in Y) = 0.0769973 s +percentage of chemistry = 87.3015 % +percentage of rho/U/Y/E = 5.43745 % +========Time details of each equation======= +rhoEqn Time = 0.00039 s +rhoEqn assamble = 0.000305 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001394 s +UEqn assamble = 0.000824 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00057 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001734 s +YEqn assamble = 0.000661 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000114 s +YEqn correct boundary = 0 s +EEqn Time = 0.000472 s +EEqn assamble = 0.000355 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000117 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 271.76 s ClockTime = 272 s +Courant Number mean: 0.00131828 max: 0.0135072 +Time = 0.00205 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21831 + Current mass in system = 1.12941e-09 + Linear momentum = (1.71343e-11 -4.80456e-09 0) + |Linear momentum| = 4.80459e-09 + Linear kinetic energy = 1.16133e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 447.094, 540.2 + Mass transfer phase change = 5.7673e-10 + D10, D32, Dmax (mu) = 49.0279, 71.6377, 179.213 + Liquid penetration 95% mass (m) = 0.0133682 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0217889, Final residual = 9.10348e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.11639, Final residual = 2.72072e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000626735, Final residual = 4.21506e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000328539, Final residual = 2.10181e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000368882, Final residual = 2.71924e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000368851, Final residual = 2.72833e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000515919, Final residual = 3.26609e-08, No Iterations 1 +min/max(T) = 806.45, 2738.26 +GAMG: Solving for p, Initial residual = 0.00968899, Final residual = 8.56671e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.06425e-05, global = 1.99808e-05, cumulative = 0.0131877 +GAMG: Solving for p, Initial residual = 8.23531e-05, Final residual = 7.19003e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.01056e-05, global = 2.01013e-05, cumulative = 0.0132078 +smoothSolver: Solving for epsilon, Initial residual = 0.000740757, Final residual = 7.64679e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000739817, Final residual = 1.06785e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.11376 s +other Time = 0 s +rho Equations = 0.00018 s +U Equations = 0.001207 s +Y Equations = 0.00274699 s +E Equations = 0.000664 s +p Equations = 0.002203 s +calculate parcels = 191.589 s +chemistry correctThermo = 0.003037 s +turbulence correct = 0.001126 s +combustion correct(in Y) = 0.10239 s +percentage of chemistry = 90.0053 % +percentage of rho/U/Y/E = 4.21764 % +========Time details of each equation======= +rhoEqn Time = 0.000337 s +rhoEqn assamble = 0.000266 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001206 s +UEqn assamble = 0.000711 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000495 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002095 s +YEqn assamble = 0.000761 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000255 s +YEqn correct boundary = 0 s +EEqn Time = 0.000497 s +EEqn assamble = 0.000382 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 272.21 s ClockTime = 273 s +Courant Number mean: 0.00125453 max: 0.0135354 +Time = 0.0020525 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21828 + Current mass in system = 1.12768e-09 + Linear momentum = (1.71842e-11 -4.79399e-09 0) + |Linear momentum| = 4.79402e-09 + Linear kinetic energy = 1.15799e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 447.303, 540.2 + Mass transfer phase change = 5.78461e-10 + D10, D32, Dmax (mu) = 49.0321, 71.5814, 179.708 + Liquid penetration 95% mass (m) = 0.0133761 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0222249, Final residual = 9.43241e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.119186, Final residual = 2.75752e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000630843, Final residual = 4.30336e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00033462, Final residual = 2.13407e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000375335, Final residual = 2.79178e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000375302, Final residual = 2.8013e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000515537, Final residual = 3.3125e-08, No Iterations 1 +min/max(T) = 806.451, 2739.07 +GAMG: Solving for p, Initial residual = 0.00910916, Final residual = 7.78476e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.04471e-05, global = 1.98197e-05, cumulative = 0.0132277 +GAMG: Solving for p, Initial residual = 7.49282e-05, Final residual = 6.85922e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.99533e-05, global = 1.99489e-05, cumulative = 0.0132476 +smoothSolver: Solving for epsilon, Initial residual = 0.000753372, Final residual = 7.81887e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00074591, Final residual = 1.08295e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.1105 s +other Time = 0 s +rho Equations = 0.00018 s +U Equations = 0.001175 s +Y Equations = 0.00253448 s +E Equations = 0.000609 s +p Equations = 0.002027 s +calculate parcels = 191.955 s +chemistry correctThermo = 0.002939 s +turbulence correct = 0.001009 s +combustion correct(in Y) = 0.0998215 s +percentage of chemistry = 90.3362 % +percentage of rho/U/Y/E = 4.07102 % +========Time details of each equation======= +rhoEqn Time = 0.00032 s +rhoEqn assamble = 0.00025 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001173 s +UEqn assamble = 0.000677 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000496 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001882 s +YEqn assamble = 0.000695 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000193 s +YEqn correct boundary = 0 s +EEqn Time = 0.000448 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 272.69 s ClockTime = 273 s +Courant Number mean: 0.00121967 max: 0.0135749 +Time = 0.002055 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21827 + Current mass in system = 1.12597e-09 + Linear momentum = (1.72444e-11 -4.78379e-09 0) + |Linear momentum| = 4.78382e-09 + Linear kinetic energy = 1.15477e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 447.512, 540.2 + Mass transfer phase change = 5.80168e-10 + D10, D32, Dmax (mu) = 48.985, 71.5249, 180.199 + Liquid penetration 95% mass (m) = 0.0133847 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0212733, Final residual = 9.02337e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.120568, Final residual = 2.77535e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000628354, Final residual = 4.32572e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000340155, Final residual = 2.16883e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000382528, Final residual = 2.86402e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000382498, Final residual = 2.87359e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000514765, Final residual = 3.35034e-08, No Iterations 1 +min/max(T) = 806.454, 2739.87 +GAMG: Solving for p, Initial residual = 0.00857229, Final residual = 8.06986e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.02288e-05, global = 1.95195e-05, cumulative = 0.0132671 +GAMG: Solving for p, Initial residual = 7.79357e-05, Final residual = 7.21785e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.96855e-05, global = 1.96799e-05, cumulative = 0.0132868 +smoothSolver: Solving for epsilon, Initial residual = 0.000763565, Final residual = 7.95549e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000750625, Final residual = 1.09908e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.088066 s +other Time = 0 s +rho Equations = 0.000182 s +U Equations = 0.001238 s +Y Equations = 0.00280843 s +E Equations = 0.000645 s +p Equations = 0.002391 s +calculate parcels = 192.248 s +chemistry correctThermo = 0.00313 s +turbulence correct = 0.000923 s +combustion correct(in Y) = 0.0765546 s +percentage of chemistry = 86.9286 % +percentage of rho/U/Y/E = 5.53383 % +========Time details of each equation======= +rhoEqn Time = 0.00037 s +rhoEqn assamble = 0.000295 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001235 s +UEqn assamble = 0.000725 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00051 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002176 s +YEqn assamble = 0.000736 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000262 s +YEqn correct boundary = 0 s +EEqn Time = 0.000478 s +EEqn assamble = 0.000358 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00012 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 273.07 s ClockTime = 274 s +Courant Number mean: 0.00121098 max: 0.0136854 +Time = 0.0020575 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21827 + Current mass in system = 1.12428e-09 + Linear momentum = (1.7319e-11 -4.77389e-09 0) + |Linear momentum| = 4.77392e-09 + Linear kinetic energy = 1.15166e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 447.722, 540.2 + Mass transfer phase change = 5.8186e-10 + D10, D32, Dmax (mu) = 48.9219, 71.4695, 180.682 + Liquid penetration 95% mass (m) = 0.0133922 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0200248, Final residual = 8.51265e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.119131, Final residual = 2.74246e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000626371, Final residual = 4.34087e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00034472, Final residual = 2.21463e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000389338, Final residual = 2.9414e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00038932, Final residual = 2.95106e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000513047, Final residual = 3.37386e-08, No Iterations 1 +min/max(T) = 806.458, 2740.65 +GAMG: Solving for p, Initial residual = 0.00802234, Final residual = 7.59044e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.00346e-05, global = 1.93213e-05, cumulative = 0.0133061 +GAMG: Solving for p, Initial residual = 7.32497e-05, Final residual = 6.15085e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.95009e-05, global = 1.94958e-05, cumulative = 0.0133256 +smoothSolver: Solving for epsilon, Initial residual = 0.000772782, Final residual = 8.08589e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000754835, Final residual = 1.11555e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.081151 s +other Time = 0 s +rho Equations = 0.00016 s +U Equations = 0.001138 s +Y Equations = 0.00215363 s +E Equations = 0.0005 s +p Equations = 0.001788 s +calculate parcels = 192.569 s +chemistry correctThermo = 0.003222 s +turbulence correct = 0.000862 s +combustion correct(in Y) = 0.0711364 s +percentage of chemistry = 87.6593 % +percentage of rho/U/Y/E = 4.86948 % +========Time details of each equation======= +rhoEqn Time = 0.000287 s +rhoEqn assamble = 0.000224 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001138 s +UEqn assamble = 0.000683 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000455 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001562 s +YEqn assamble = 0.00055 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000144 s +YEqn correct boundary = 0 s +EEqn Time = 0.000381 s +EEqn assamble = 0.000284 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.7e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 273.47 s ClockTime = 274 s +Courant Number mean: 0.00122761 max: 0.0143702 +Time = 0.00206 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21827 + Current mass in system = 1.1226e-09 + Linear momentum = (1.74099e-11 -4.76423e-09 0) + |Linear momentum| = 4.76426e-09 + Linear kinetic energy = 1.14863e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 447.934, 540.2 + Mass transfer phase change = 5.83541e-10 + D10, D32, Dmax (mu) = 48.8608, 71.4158, 181.156 + Liquid penetration 95% mass (m) = 0.0133993 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0181899, Final residual = 7.8752e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.110593, Final residual = 2.56078e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000626672, Final residual = 4.38138e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000348408, Final residual = 2.25111e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00039473, Final residual = 2.99031e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000394715, Final residual = 2.99989e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000512247, Final residual = 3.3984e-08, No Iterations 1 +min/max(T) = 806.463, 2741.4 +GAMG: Solving for p, Initial residual = 0.00753938, Final residual = 7.37524e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.98648e-05, global = 1.91725e-05, cumulative = 0.0133448 +GAMG: Solving for p, Initial residual = 7.14136e-05, Final residual = 5.21437e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.93789e-05, global = 1.93747e-05, cumulative = 0.0133642 +smoothSolver: Solving for epsilon, Initial residual = 0.000781581, Final residual = 8.21632e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000757928, Final residual = 1.13093e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102536 s +other Time = 0 s +rho Equations = 0.000179 s +U Equations = 0.001313 s +Y Equations = 0.00211693 s +E Equations = 0.000492 s +p Equations = 0.003163 s +calculate parcels = 192.919 s +chemistry correctThermo = 0.002015 s +turbulence correct = 0.001701 s +combustion correct(in Y) = 0.0913451 s +percentage of chemistry = 89.0859 % +percentage of rho/U/Y/E = 3.9995 % +========Time details of each equation======= +rhoEqn Time = 0.000464 s +rhoEqn assamble = 0.000352 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000112 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001313 s +UEqn assamble = 0.000805 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000508 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001475 s +YEqn assamble = 0.000527 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000114 s +YEqn correct boundary = 0 s +EEqn Time = 0.000366 s +EEqn assamble = 0.000272 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 273.92 s ClockTime = 274 s +Courant Number mean: 0.0012693 max: 0.014788 +Time = 0.0020625 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21825 + Current mass in system = 1.12092e-09 + Linear momentum = (1.75176e-11 -4.7548e-09 0) + |Linear momentum| = 4.75483e-09 + Linear kinetic energy = 1.14569e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 448.147, 540.2 + Mass transfer phase change = 5.85219e-10 + D10, D32, Dmax (mu) = 48.859, 71.3664, 181.617 + Liquid penetration 95% mass (m) = 0.0134068 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0155662, Final residual = 6.86026e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.101473, Final residual = 2.37515e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000627636, Final residual = 4.39422e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00035131, Final residual = 2.29023e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000398268, Final residual = 3.03145e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000398255, Final residual = 3.04108e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00051168, Final residual = 3.41777e-08, No Iterations 1 +min/max(T) = 806.47, 2742.13 +GAMG: Solving for p, Initial residual = 0.00708923, Final residual = 7.59399e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.98103e-05, global = 1.91143e-05, cumulative = 0.0133833 +GAMG: Solving for p, Initial residual = 7.3786e-05, Final residual = 5.16313e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.93435e-05, global = 1.93395e-05, cumulative = 0.0134026 +smoothSolver: Solving for epsilon, Initial residual = 0.000789559, Final residual = 8.34932e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000760463, Final residual = 1.14643e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.106877 s +other Time = 1e-06 s +rho Equations = 0.000176 s +U Equations = 0.001172 s +Y Equations = 0.0026445 s +E Equations = 0.000599 s +p Equations = 0.002244 s +calculate parcels = 193.282 s +chemistry correctThermo = 0.002902 s +turbulence correct = 0.001005 s +combustion correct(in Y) = 0.0959325 s +percentage of chemistry = 89.7597 % +percentage of rho/U/Y/E = 4.29606 % +========Time details of each equation======= +rhoEqn Time = 0.00034 s +rhoEqn assamble = 0.000269 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001171 s +UEqn assamble = 0.000659 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000512 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001996 s +YEqn assamble = 0.000669 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000199 s +YEqn correct boundary = 0 s +EEqn Time = 0.000439 s +EEqn assamble = 0.000328 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 274.39 s ClockTime = 275 s +Courant Number mean: 0.00133783 max: 0.0150435 +Time = 0.002065 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21822 + Current mass in system = 1.11923e-09 + Linear momentum = (1.76685e-11 -4.74557e-09 0) + |Linear momentum| = 4.74561e-09 + Linear kinetic energy = 1.14283e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 448.361, 540.2 + Mass transfer phase change = 5.86917e-10 + D10, D32, Dmax (mu) = 48.8504, 71.3225, 182.063 + Liquid penetration 95% mass (m) = 0.0134146 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0123539, Final residual = 5.45245e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0931669, Final residual = 2.2165e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000640693, Final residual = 4.68319e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000353291, Final residual = 2.31515e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000403682, Final residual = 3.10796e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000403699, Final residual = 3.11788e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00051108, Final residual = 3.48357e-08, No Iterations 1 +min/max(T) = 806.477, 2742.81 +GAMG: Solving for p, Initial residual = 0.00688931, Final residual = 0.000109176, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.00752e-05, global = 1.92573e-05, cumulative = 0.0134219 +GAMG: Solving for p, Initial residual = 0.00010602, Final residual = 3.3502e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.95686e-05, global = 1.9567e-05, cumulative = 0.0134414 +smoothSolver: Solving for epsilon, Initial residual = 0.000802721, Final residual = 8.48036e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000765231, Final residual = 1.16466e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09453 s +other Time = 0 s +rho Equations = 0.000221 s +U Equations = 0.001641 s +Y Equations = 0.00256097 s +E Equations = 0.000598 s +p Equations = 0.002207 s +calculate parcels = 193.65 s +chemistry correctThermo = 0.002886 s +turbulence correct = 0.000971 s +combustion correct(in Y) = 0.083214 s +percentage of chemistry = 88.0292 % +percentage of rho/U/Y/E = 5.31151 % +========Time details of each equation======= +rhoEqn Time = 0.000363 s +rhoEqn assamble = 0.000281 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00164 s +UEqn assamble = 0.000879 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000761 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001662 s +YEqn assamble = 0.000631 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 7.2e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.00044 s +EEqn assamble = 0.000326 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 274.86 s ClockTime = 275 s +Courant Number mean: 0.00143814 max: 0.0152178 +Time = 0.0020675 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21822 + Current mass in system = 1.11758e-09 + Linear momentum = (1.78321e-11 -4.73667e-09 0) + |Linear momentum| = 4.7367e-09 + Linear kinetic energy = 1.14007e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 448.577, 540.2 + Mass transfer phase change = 5.88567e-10 + D10, D32, Dmax (mu) = 48.7926, 71.273, 182.493 + Liquid penetration 95% mass (m) = 0.0134216 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0109675, Final residual = 4.86521e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0856951, Final residual = 2.0882e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000627945, Final residual = 4.46658e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000353228, Final residual = 2.33119e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000405977, Final residual = 3.11588e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000405984, Final residual = 3.12528e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000510468, Final residual = 3.47749e-08, No Iterations 1 +min/max(T) = 806.485, 2743.43 +GAMG: Solving for p, Initial residual = 0.00690766, Final residual = 0.000133924, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.97443e-05, global = 1.87831e-05, cumulative = 0.0134602 +GAMG: Solving for p, Initial residual = 0.000129094, Final residual = 4.65298e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.90187e-05, global = 1.9016e-05, cumulative = 0.0134792 +smoothSolver: Solving for epsilon, Initial residual = 0.000806946, Final residual = 8.63426e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000768888, Final residual = 1.18261e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.08784 s +other Time = 1e-06 s +rho Equations = 0.000196 s +U Equations = 0.001152 s +Y Equations = 0.0022613 s +E Equations = 0.000526 s +p Equations = 0.00197 s +calculate parcels = 193.982 s +chemistry correctThermo = 0.002 s +turbulence correct = 0.001002 s +combustion correct(in Y) = 0.0785167 s +percentage of chemistry = 89.386 % +percentage of rho/U/Y/E = 4.70777 % +========Time details of each equation======= +rhoEqn Time = 0.000322 s +rhoEqn assamble = 0.00026 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00115 s +UEqn assamble = 0.000675 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000475 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001573 s +YEqn assamble = 0.000573 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000401 s +EEqn assamble = 0.000304 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.7e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 275.28 s ClockTime = 276 s +Courant Number mean: 0.00157939 max: 0.0154599 +Time = 0.00207 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21820 + Current mass in system = 1.1159e-09 + Linear momentum = (1.79753e-11 -4.72797e-09 0) + |Linear momentum| = 4.728e-09 + Linear kinetic energy = 1.1374e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 448.793, 540.2 + Mass transfer phase change = 5.90242e-10 + D10, D32, Dmax (mu) = 48.7639, 71.2305, 182.361 + Liquid penetration 95% mass (m) = 0.0134284 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00812745, Final residual = 3.31502e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0788857, Final residual = 1.96874e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000638237, Final residual = 4.65538e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000354425, Final residual = 2.33863e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000410821, Final residual = 3.17012e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000410823, Final residual = 3.17956e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000510721, Final residual = 3.52227e-08, No Iterations 1 +min/max(T) = 806.493, 2743.98 +GAMG: Solving for p, Initial residual = 0.00687943, Final residual = 0.000121248, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.9988e-05, global = 1.90384e-05, cumulative = 0.0134983 +GAMG: Solving for p, Initial residual = 0.000117245, Final residual = 3.79184e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.93114e-05, global = 1.93086e-05, cumulative = 0.0135176 +smoothSolver: Solving for epsilon, Initial residual = 0.000817175, Final residual = 8.88246e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000773068, Final residual = 1.20889e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.096391 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001026 s +Y Equations = 0.00215632 s +E Equations = 0.000711 s +p Equations = 0.002241 s +calculate parcels = 194.248 s +chemistry correctThermo = 0.001992 s +turbulence correct = 0.001102 s +combustion correct(in Y) = 0.0868007 s +percentage of chemistry = 90.0506 % +percentage of rho/U/Y/E = 4.22272 % +========Time details of each equation======= +rhoEqn Time = 0.000328 s +rhoEqn assamble = 0.000253 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001025 s +UEqn assamble = 0.000615 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00041 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.0016 s +YEqn assamble = 0.000607 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000144 s +YEqn correct boundary = 0 s +EEqn Time = 0.000593 s +EEqn assamble = 0.000494 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 275.64 s ClockTime = 276 s +Courant Number mean: 0.00174422 max: 0.0156457 +Time = 0.0020725 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21818 + Current mass in system = 1.11423e-09 + Linear momentum = (1.80903e-11 -4.71951e-09 0) + |Linear momentum| = 4.71955e-09 + Linear kinetic energy = 1.13482e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 449.01, 540.2 + Mass transfer phase change = 5.91918e-10 + D10, D32, Dmax (mu) = 48.7434, 71.1912, 182.176 + Liquid penetration 95% mass (m) = 0.0134356 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00904072, Final residual = 4.16088e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0728105, Final residual = 1.87798e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000634245, Final residual = 4.73018e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00035493, Final residual = 2.3439e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000412829, Final residual = 3.19525e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000412823, Final residual = 3.2046e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000511001, Final residual = 3.56387e-08, No Iterations 1 +min/max(T) = 806.502, 2744.4 +GAMG: Solving for p, Initial residual = 0.0071077, Final residual = 0.00011052, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.99881e-05, global = 1.90703e-05, cumulative = 0.0135367 +GAMG: Solving for p, Initial residual = 0.000106393, Final residual = 3.22788e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.93181e-05, global = 1.93163e-05, cumulative = 0.013556 +smoothSolver: Solving for epsilon, Initial residual = 0.000821665, Final residual = 8.98511e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000777846, Final residual = 1.23111e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.114942 s +other Time = 0 s +rho Equations = 0.000179 s +U Equations = 0.001244 s +Y Equations = 0.00245343 s +E Equations = 0.000603 s +p Equations = 0.002314 s +calculate parcels = 194.615 s +chemistry correctThermo = 0.0029 s +turbulence correct = 0.001057 s +combustion correct(in Y) = 0.103986 s +percentage of chemistry = 90.4679 % +percentage of rho/U/Y/E = 3.89712 % +========Time details of each equation======= +rhoEqn Time = 0.000323 s +rhoEqn assamble = 0.000254 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001243 s +UEqn assamble = 0.000731 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000512 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001798 s +YEqn assamble = 0.000625 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000183 s +YEqn correct boundary = 0 s +EEqn Time = 0.000448 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 276.12 s ClockTime = 277 s +Courant Number mean: 0.00190764 max: 0.0157197 +Time = 0.002075 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21817 + Current mass in system = 1.1126e-09 + Linear momentum = (1.82093e-11 -4.71136e-09 0) + |Linear momentum| = 4.7114e-09 + Linear kinetic energy = 1.13233e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 449.229, 540.2 + Mass transfer phase change = 5.93543e-10 + D10, D32, Dmax (mu) = 48.7049, 71.1461, 181.993 + Liquid penetration 95% mass (m) = 0.0134426 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00842078, Final residual = 3.2124e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.067303, Final residual = 1.78823e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000631283, Final residual = 4.59218e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000354759, Final residual = 2.35268e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000415689, Final residual = 3.20722e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000415679, Final residual = 3.21637e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000518546, Final residual = 3.61825e-08, No Iterations 1 +min/max(T) = 806.51, 2744.78 +GAMG: Solving for p, Initial residual = 0.00756357, Final residual = 0.000123876, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.95805e-05, global = 1.85275e-05, cumulative = 0.0135745 +GAMG: Solving for p, Initial residual = 0.000119089, Final residual = 3.99862e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.87299e-05, global = 1.87276e-05, cumulative = 0.0135932 +smoothSolver: Solving for epsilon, Initial residual = 0.000824594, Final residual = 9.04487e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000784555, Final residual = 1.25354e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102378 s +other Time = 0 s +rho Equations = 0.000149 s +U Equations = 0.000986 s +Y Equations = 0.00205784 s +E Equations = 0.000484 s +p Equations = 0.001928 s +calculate parcels = 194.961 s +chemistry correctThermo = 0.002156 s +turbulence correct = 0.000838 s +combustion correct(in Y) = 0.0935952 s +percentage of chemistry = 91.4212 % +percentage of rho/U/Y/E = 3.59144 % +========Time details of each equation======= +rhoEqn Time = 0.00028 s +rhoEqn assamble = 0.000221 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000984 s +UEqn assamble = 0.000568 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000416 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00151 s +YEqn assamble = 0.000526 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000142 s +YEqn correct boundary = 0 s +EEqn Time = 0.000365 s +EEqn assamble = 0.000273 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 276.57 s ClockTime = 277 s +Courant Number mean: 0.00206737 max: 0.0157373 +Time = 0.0020775 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21813 + Current mass in system = 1.11096e-09 + Linear momentum = (1.83376e-11 -4.70339e-09 0) + |Linear momentum| = 4.70343e-09 + Linear kinetic energy = 1.12993e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 449.448, 540.2 + Mass transfer phase change = 5.9518e-10 + D10, D32, Dmax (mu) = 48.737, 71.108, 181.811 + Liquid penetration 95% mass (m) = 0.0134497 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00978525, Final residual = 3.82556e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0625612, Final residual = 1.70204e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000629635, Final residual = 4.62587e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000357103, Final residual = 2.37223e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000418414, Final residual = 3.24705e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000418402, Final residual = 3.25642e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000522107, Final residual = 3.65924e-08, No Iterations 1 +min/max(T) = 806.517, 2745.3 +GAMG: Solving for p, Initial residual = 0.00809071, Final residual = 0.000109433, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.95775e-05, global = 1.87318e-05, cumulative = 0.013612 +GAMG: Solving for p, Initial residual = 0.000104894, Final residual = 2.8831e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.88759e-05, global = 1.8874e-05, cumulative = 0.0136308 +smoothSolver: Solving for epsilon, Initial residual = 0.00082716, Final residual = 9.17134e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000788997, Final residual = 1.27498e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.108907 s +other Time = 1e-06 s +rho Equations = 0.000158 s +U Equations = 0.000978 s +Y Equations = 0.00242731 s +E Equations = 0.0006 s +p Equations = 0.002585 s +calculate parcels = 195.305 s +chemistry correctThermo = 0.002966 s +turbulence correct = 0.001043 s +combustion correct(in Y) = 0.0979387 s +percentage of chemistry = 89.9287 % +percentage of rho/U/Y/E = 3.82281 % +========Time details of each equation======= +rhoEqn Time = 0.000324 s +rhoEqn assamble = 0.000255 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000978 s +UEqn assamble = 0.000566 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000412 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001874 s +YEqn assamble = 0.000648 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000244 s +YEqn correct boundary = 0 s +EEqn Time = 0.000444 s +EEqn assamble = 0.000329 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 277.02 s ClockTime = 278 s +Courant Number mean: 0.00222625 max: 0.0156581 +Time = 0.00208 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21811 + Current mass in system = 1.10934e-09 + Linear momentum = (1.84777e-11 -4.69566e-09 0) + |Linear momentum| = 4.69569e-09 + Linear kinetic energy = 1.12759e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 449.656, 540.2 + Mass transfer phase change = 5.96802e-10 + D10, D32, Dmax (mu) = 48.7212, 71.0674, 181.631 + Liquid penetration 95% mass (m) = 0.0134572 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00885301, Final residual = 3.58125e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0583304, Final residual = 1.63283e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000624303, Final residual = 4.62353e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000359667, Final residual = 2.40037e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000424199, Final residual = 3.30612e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000424181, Final residual = 3.31534e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000529032, Final residual = 3.70934e-08, No Iterations 1 +min/max(T) = 806.521, 2745.87 +GAMG: Solving for p, Initial residual = 0.00859248, Final residual = 9.46651e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.93938e-05, global = 1.85679e-05, cumulative = 0.0136494 +GAMG: Solving for p, Initial residual = 9.15201e-05, Final residual = 9.11819e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.87027e-05, global = 1.86964e-05, cumulative = 0.0136681 +smoothSolver: Solving for epsilon, Initial residual = 0.000830492, Final residual = 9.32867e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000793394, Final residual = 1.29899e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.110818 s +other Time = 0 s +rho Equations = 0.000181 s +U Equations = 0.001243 s +Y Equations = 0.00240718 s +E Equations = 0.000593 s +p Equations = 0.002036 s +calculate parcels = 195.639 s +chemistry correctThermo = 0.002906 s +turbulence correct = 0.000973 s +combustion correct(in Y) = 0.100281 s +percentage of chemistry = 90.4915 % +percentage of rho/U/Y/E = 3.9923 % +========Time details of each equation======= +rhoEqn Time = 0.000324 s +rhoEqn assamble = 0.000256 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001241 s +UEqn assamble = 0.000733 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000508 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001763 s +YEqn assamble = 0.000624 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000182 s +YEqn correct boundary = 0 s +EEqn Time = 0.000442 s +EEqn assamble = 0.000328 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 277.47 s ClockTime = 278 s +Courant Number mean: 0.00238617 max: 0.0155973 +Time = 0.0020825 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21809 + Current mass in system = 1.10773e-09 + Linear momentum = (1.86298e-11 -4.68811e-09 0) + |Linear momentum| = 4.68815e-09 + Linear kinetic energy = 1.12532e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 449.82, 540.2 + Mass transfer phase change = 5.98411e-10 + D10, D32, Dmax (mu) = 48.7062, 71.0252, 181.452 + Liquid penetration 95% mass (m) = 0.0134642 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00895879, Final residual = 4.1336e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0545835, Final residual = 1.57326e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00062823, Final residual = 4.69115e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000361423, Final residual = 2.43773e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000429218, Final residual = 3.36645e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000429199, Final residual = 3.3757e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000539394, Final residual = 3.77755e-08, No Iterations 1 +min/max(T) = 806.525, 2746.32 +GAMG: Solving for p, Initial residual = 0.00922713, Final residual = 9.46839e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.92328e-05, global = 1.84242e-05, cumulative = 0.0136865 +GAMG: Solving for p, Initial residual = 9.15514e-05, Final residual = 9.01515e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.8551e-05, global = 1.85455e-05, cumulative = 0.0137051 +smoothSolver: Solving for epsilon, Initial residual = 0.000837671, Final residual = 9.51492e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000797982, Final residual = 1.32468e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.07954 s +other Time = 2e-06 s +rho Equations = 0.000225 s +U Equations = 0.001459 s +Y Equations = 0.00216864 s +E Equations = 0.00048 s +p Equations = 0.001796 s +calculate parcels = 195.958 s +chemistry correctThermo = 0.001957 s +turbulence correct = 0.000845 s +combustion correct(in Y) = 0.0703444 s +percentage of chemistry = 88.439 % +percentage of rho/U/Y/E = 5.44713 % +========Time details of each equation======= +rhoEqn Time = 0.000345 s +rhoEqn assamble = 0.000274 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001457 s +UEqn assamble = 0.000882 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000575 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001457 s +YEqn assamble = 0.000523 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 5.8e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000361 s +EEqn assamble = 0.000271 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 277.86 s ClockTime = 278 s +Courant Number mean: 0.00254668 max: 0.0160113 +Time = 0.002085 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21807 + Current mass in system = 1.10612e-09 + Linear momentum = (1.88003e-11 -4.68071e-09 0) + |Linear momentum| = 4.68074e-09 + Linear kinetic energy = 1.12311e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 449.985, 540.2 + Mass transfer phase change = 6.00018e-10 + D10, D32, Dmax (mu) = 48.6899, 70.9824, 181.273 + Liquid penetration 95% mass (m) = 0.0134711 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0106323, Final residual = 5.27943e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0512074, Final residual = 1.51596e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000629847, Final residual = 4.70909e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00036405, Final residual = 2.48466e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000434181, Final residual = 3.43047e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000434161, Final residual = 3.43978e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000548825, Final residual = 3.83004e-08, No Iterations 1 +min/max(T) = 806.53, 2746.78 +GAMG: Solving for p, Initial residual = 0.00991948, Final residual = 8.42693e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.91133e-05, global = 1.83932e-05, cumulative = 0.0137235 +GAMG: Solving for p, Initial residual = 8.22573e-05, Final residual = 6.24631e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.85241e-05, global = 1.85198e-05, cumulative = 0.013742 +smoothSolver: Solving for epsilon, Initial residual = 0.000842564, Final residual = 9.65766e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000800974, Final residual = 1.34768e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.10942 s +other Time = 0 s +rho Equations = 0.000244 s +U Equations = 0.001689 s +Y Equations = 0.00233034 s +E Equations = 0.000496 s +p Equations = 0.00212 s +calculate parcels = 196.271 s +chemistry correctThermo = 0.002055 s +turbulence correct = 0.00096 s +combustion correct(in Y) = 0.0992457 s +percentage of chemistry = 90.7016 % +percentage of rho/U/Y/E = 4.34961 % +========Time details of each equation======= +rhoEqn Time = 0.000397 s +rhoEqn assamble = 0.000305 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001688 s +UEqn assamble = 0.00092 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000768 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001232 s +YEqn assamble = 0.000529 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -0.000131 s +YEqn correct boundary = 0 s +EEqn Time = 0.000373 s +EEqn assamble = 0.000279 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 278.29 s ClockTime = 279 s +Courant Number mean: 0.0027075 max: 0.0162919 +Time = 0.0020875 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21805 + Current mass in system = 1.10449e-09 + Linear momentum = (1.90026e-11 -4.67337e-09 0) + |Linear momentum| = 4.67341e-09 + Linear kinetic energy = 1.12093e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 450.149, 540.2 + Mass transfer phase change = 6.0165e-10 + D10, D32, Dmax (mu) = 48.6638, 70.9442, 181.096 + Liquid penetration 95% mass (m) = 0.0134794 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.011748, Final residual = 6.05891e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0481303, Final residual = 1.4631e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000635103, Final residual = 4.83888e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000366234, Final residual = 2.54444e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00043798, Final residual = 3.49613e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00043797, Final residual = 3.50599e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000556265, Final residual = 3.88827e-08, No Iterations 1 +min/max(T) = 806.536, 2747.23 +GAMG: Solving for p, Initial residual = 0.0107387, Final residual = 9.59741e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.93284e-05, global = 1.8638e-05, cumulative = 0.0137606 +GAMG: Solving for p, Initial residual = 9.39093e-05, Final residual = 1.98541e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.88089e-05, global = 1.8808e-05, cumulative = 0.0137794 +smoothSolver: Solving for epsilon, Initial residual = 0.000843631, Final residual = 9.77107e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00080241, Final residual = 1.37064e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.096036 s +other Time = 0 s +rho Equations = 0.000217 s +U Equations = 0.001225 s +Y Equations = 0.00210824 s +E Equations = 0.000513 s +p Equations = 0.002332 s +calculate parcels = 196.617 s +chemistry correctThermo = 0.002812 s +turbulence correct = 0.001096 s +combustion correct(in Y) = 0.0855188 s +percentage of chemistry = 89.0486 % +percentage of rho/U/Y/E = 4.23096 % +========Time details of each equation======= +rhoEqn Time = 0.000377 s +rhoEqn assamble = 0.000298 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001224 s +UEqn assamble = 0.000716 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000508 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001423 s +YEqn assamble = 0.000522 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 6.6e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000394 s +EEqn assamble = 0.000274 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00012 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 278.73 s ClockTime = 279 s +Courant Number mean: 0.00286923 max: 0.0165353 +Time = 0.00209 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21803 + Current mass in system = 1.10281e-09 + Linear momentum = (1.92768e-11 -4.66614e-09 0) + |Linear momentum| = 4.66618e-09 + Linear kinetic energy = 1.11879e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 450.314, 540.2 + Mass transfer phase change = 6.03329e-10 + D10, D32, Dmax (mu) = 48.6046, 70.9056, 180.921 + Liquid penetration 95% mass (m) = 0.0134866 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0132221, Final residual = 6.72428e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0453634, Final residual = 1.41478e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000665743, Final residual = 5.03408e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000367158, Final residual = 2.61211e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000448385, Final residual = 3.60703e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000448375, Final residual = 3.617e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000573227, Final residual = 3.98141e-08, No Iterations 1 +min/max(T) = 806.544, 2747.65 +GAMG: Solving for p, Initial residual = 0.0119563, Final residual = 0.000183037, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.01197e-05, global = 1.90937e-05, cumulative = 0.0137985 +GAMG: Solving for p, Initial residual = 0.000181707, Final residual = 5.817e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.93598e-05, global = 1.93576e-05, cumulative = 0.0138179 +smoothSolver: Solving for epsilon, Initial residual = 0.000860109, Final residual = 9.93661e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00081308, Final residual = 1.40199e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.110475 s +other Time = 0 s +rho Equations = 0.000186 s +U Equations = 0.001197 s +Y Equations = 0.00256136 s +E Equations = 0.0006 s +p Equations = 0.002264 s +calculate parcels = 196.955 s +chemistry correctThermo = 0.002874 s +turbulence correct = 0.000994 s +combustion correct(in Y) = 0.0995996 s +percentage of chemistry = 90.1558 % +percentage of rho/U/Y/E = 4.11348 % +========Time details of each equation======= +rhoEqn Time = 0.000331 s +rhoEqn assamble = 0.000262 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001195 s +UEqn assamble = 0.000689 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000506 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001819 s +YEqn assamble = 0.000653 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000171 s +YEqn correct boundary = 0 s +EEqn Time = 0.000446 s +EEqn assamble = 0.000333 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 279.18 s ClockTime = 280 s +Courant Number mean: 0.00303313 max: 0.0166474 +Time = 0.0020925 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21801 + Current mass in system = 1.10113e-09 + Linear momentum = (1.95676e-11 -4.65886e-09 0) + |Linear momentum| = 4.6589e-09 + Linear kinetic energy = 1.11665e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 450.477, 540.2 + Mass transfer phase change = 6.05009e-10 + D10, D32, Dmax (mu) = 48.5546, 70.8693, 180.747 + Liquid penetration 95% mass (m) = 0.0134945 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0176016, Final residual = 9.65775e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0430626, Final residual = 1.37776e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000662128, Final residual = 5.07813e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000365214, Final residual = 2.6885e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00044626, Final residual = 3.70693e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000446261, Final residual = 3.71704e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000582927, Final residual = 4.06091e-08, No Iterations 1 +min/max(T) = 806.552, 2747.99 +GAMG: Solving for p, Initial residual = 0.0135263, Final residual = 0.000249502, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.08962e-05, global = 1.91717e-05, cumulative = 0.0138371 +GAMG: Solving for p, Initial residual = 0.000247114, Final residual = 2.67786e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.93651e-05, global = 1.93631e-05, cumulative = 0.0138564 +smoothSolver: Solving for epsilon, Initial residual = 0.000853541, Final residual = 9.98181e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000809431, Final residual = 1.41972e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.111008 s +other Time = 0 s +rho Equations = 0.000201 s +U Equations = 0.001173 s +Y Equations = 0.00253238 s +E Equations = 0.000597 s +p Equations = 0.002521 s +calculate parcels = 197.31 s +chemistry correctThermo = 0.00288 s +turbulence correct = 0.001111 s +combustion correct(in Y) = 0.0997876 s +percentage of chemistry = 89.8923 % +percentage of rho/U/Y/E = 4.0568 % +========Time details of each equation======= +rhoEqn Time = 0.000357 s +rhoEqn assamble = 0.000272 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00117 s +UEqn assamble = 0.000677 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000493 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001902 s +YEqn assamble = 0.000664 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00023 s +YEqn correct boundary = 0 s +EEqn Time = 0.000441 s +EEqn assamble = 0.000331 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00011 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 279.64 s ClockTime = 280 s +Courant Number mean: 0.00319414 max: 0.0165562 +Time = 0.002095 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21799 + Current mass in system = 1.09949e-09 + Linear momentum = (1.97989e-11 -4.65165e-09 0) + |Linear momentum| = 4.65169e-09 + Linear kinetic energy = 1.11453e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 450.639, 540.2 + Mass transfer phase change = 6.06655e-10 + D10, D32, Dmax (mu) = 48.5049, 70.8301, 180.576 + Liquid penetration 95% mass (m) = 0.0135021 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0169391, Final residual = 8.72081e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0407759, Final residual = 1.33072e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000639673, Final residual = 4.7156e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000363975, Final residual = 2.73074e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000444059, Final residual = 3.69754e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000444062, Final residual = 3.70815e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000587236, Final residual = 4.00699e-08, No Iterations 1 +min/max(T) = 806.56, 2748.04 +GAMG: Solving for p, Initial residual = 0.0144169, Final residual = 0.000238422, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.02566e-05, global = 1.88113e-05, cumulative = 0.0138752 +GAMG: Solving for p, Initial residual = 0.000234668, Final residual = 2.71532e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.89699e-05, global = 1.89685e-05, cumulative = 0.0138942 +smoothSolver: Solving for epsilon, Initial residual = 0.00084588, Final residual = 1.00736e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000809207, Final residual = 1.44057e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097053 s +other Time = 0 s +rho Equations = 0.000209 s +U Equations = 0.001266 s +Y Equations = 0.00231789 s +E Equations = 0.000498 s +p Equations = 0.002132 s +calculate parcels = 197.656 s +chemistry correctThermo = 0.002071 s +turbulence correct = 0.000855 s +combustion correct(in Y) = 0.0875021 s +percentage of chemistry = 90.1591 % +percentage of rho/U/Y/E = 4.42118 % +========Time details of each equation======= +rhoEqn Time = 0.000343 s +rhoEqn assamble = 0.000274 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001266 s +UEqn assamble = 0.000758 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000508 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001673 s +YEqn assamble = 0.000558 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000111 s +YEqn correct boundary = 0 s +EEqn Time = 0.000371 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 280.09 s ClockTime = 281 s +Courant Number mean: 0.00334843 max: 0.016323 +Time = 0.0020975 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21797 + Current mass in system = 1.09788e-09 + Linear momentum = (1.99863e-11 -4.64442e-09 0) + |Linear momentum| = 4.64446e-09 + Linear kinetic energy = 1.11242e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 450.798, 540.2 + Mass transfer phase change = 6.08266e-10 + D10, D32, Dmax (mu) = 48.4753, 70.7924, 180.409 + Liquid penetration 95% mass (m) = 0.0135096 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0185768, Final residual = 1.02619e-09, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0386739, Final residual = 1.27988e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000614941, Final residual = 4.55445e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000366147, Final residual = 2.79092e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000443224, Final residual = 3.73099e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000443216, Final residual = 3.74156e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000589571, Final residual = 4.02997e-08, No Iterations 1 +min/max(T) = 806.568, 2747.93 +GAMG: Solving for p, Initial residual = 0.0152052, Final residual = 0.00028064, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.01585e-05, global = 1.8435e-05, cumulative = 0.0139126 +GAMG: Solving for p, Initial residual = 0.000271965, Final residual = 2.70865e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.85696e-05, global = 1.85685e-05, cumulative = 0.0139312 +smoothSolver: Solving for epsilon, Initial residual = 0.000838968, Final residual = 1.00307e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000807687, Final residual = 1.45243e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092872 s +other Time = 0 s +rho Equations = 0.000179 s +U Equations = 0.001026 s +Y Equations = 0.00237396 s +E Equations = 0.000613 s +p Equations = 0.002423 s +calculate parcels = 197.91 s +chemistry correctThermo = 0.002869 s +turbulence correct = 0.000984 s +combustion correct(in Y) = 0.082205 s +percentage of chemistry = 88.5143 % +percentage of rho/U/Y/E = 4.51369 % +========Time details of each equation======= +rhoEqn Time = 0.000322 s +rhoEqn assamble = 0.000242 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001025 s +UEqn assamble = 0.000608 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000417 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001822 s +YEqn assamble = 0.00064 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000221 s +YEqn correct boundary = 0 s +EEqn Time = 0.00046 s +EEqn assamble = 0.000331 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000129 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 280.44 s ClockTime = 281 s +Courant Number mean: 0.00349615 max: 0.0161088 +Time = 0.0021 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21794 + Current mass in system = 1.09624e-09 + Linear momentum = (2.0148e-11 -4.63722e-09 0) + |Linear momentum| = 4.63726e-09 + Linear kinetic energy = 1.1103e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 450.959, 540.2 + Mass transfer phase change = 6.09901e-10 + D10, D32, Dmax (mu) = 48.4428, 70.7546, 180.244 + Liquid penetration 95% mass (m) = 0.0135176 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0164765, Final residual = 8.19885e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0366343, Final residual = 1.22546e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000624792, Final residual = 4.58102e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000369712, Final residual = 2.86589e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000452374, Final residual = 3.83863e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000452354, Final residual = 3.8493e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000598337, Final residual = 4.07464e-08, No Iterations 1 +min/max(T) = 806.576, 2748.19 +GAMG: Solving for p, Initial residual = 0.0161879, Final residual = 0.000256819, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.02856e-05, global = 1.87001e-05, cumulative = 0.0139499 +GAMG: Solving for p, Initial residual = 0.000252401, Final residual = 8.46888e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.88424e-05, global = 1.88389e-05, cumulative = 0.0139687 +smoothSolver: Solving for epsilon, Initial residual = 0.000840655, Final residual = 1.00575e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000809483, Final residual = 1.46906e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.082996 s +other Time = 0 s +rho Equations = 0.000156 s +U Equations = 0.00098 s +Y Equations = 0.00207607 s +E Equations = 0.00053 s +p Equations = 0.001938 s +calculate parcels = 198.254 s +chemistry correctThermo = 0.002047 s +turbulence correct = 0.000931 s +combustion correct(in Y) = 0.0741549 s +percentage of chemistry = 89.3476 % +percentage of rho/U/Y/E = 4.50874 % +========Time details of each equation======= +rhoEqn Time = 0.000276 s +rhoEqn assamble = 0.000219 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000979 s +UEqn assamble = 0.00057 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000409 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00148 s +YEqn assamble = 0.000521 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000106 s +YEqn correct boundary = 0 s +EEqn Time = 0.000412 s +EEqn assamble = 0.000314 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 281.16 s ClockTime = 282 s +Courant Number mean: 0.00364431 max: 0.0163771 +Time = 0.0021025 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21791 + Current mass in system = 1.09462e-09 + Linear momentum = (2.02367e-11 -4.63003e-09 0) + |Linear momentum| = 4.63007e-09 + Linear kinetic energy = 1.10819e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 451.121, 540.2 + Mass transfer phase change = 6.11528e-10 + D10, D32, Dmax (mu) = 48.4222, 70.7168, 180.078 + Liquid penetration 95% mass (m) = 0.0135253 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0158047, Final residual = 8.11103e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0349652, Final residual = 1.19641e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000622777, Final residual = 4.57582e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000371639, Final residual = 2.94857e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000455009, Final residual = 3.95712e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000454999, Final residual = 3.96818e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000604917, Final residual = 4.13956e-08, No Iterations 1 +min/max(T) = 806.582, 2748.7 +GAMG: Solving for p, Initial residual = 0.0172399, Final residual = 0.000298048, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.04362e-05, global = 1.86152e-05, cumulative = 0.0139874 +GAMG: Solving for p, Initial residual = 0.000292223, Final residual = 2.95431e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.8752e-05, global = 1.87501e-05, cumulative = 0.0140061 +smoothSolver: Solving for epsilon, Initial residual = 0.000833246, Final residual = 1.00704e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000809349, Final residual = 1.48443e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095823 s +other Time = 0 s +rho Equations = 0.000193 s +U Equations = 0.001251 s +Y Equations = 0.00206784 s +E Equations = 0.000467 s +p Equations = 0.001963 s +calculate parcels = 198.622 s +chemistry correctThermo = 0.002019 s +turbulence correct = 0.000873 s +combustion correct(in Y) = 0.0867912 s +percentage of chemistry = 90.5745 % +percentage of rho/U/Y/E = 4.15228 % +========Time details of each equation======= +rhoEqn Time = 0.000306 s +rhoEqn assamble = 0.000243 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001249 s +UEqn assamble = 0.000739 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00051 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001402 s +YEqn assamble = 0.000504 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 7.4e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000354 s +EEqn assamble = 0.000264 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 281.63 s ClockTime = 282 s +Courant Number mean: 0.0037928 max: 0.0168465 +Time = 0.002105 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21791 + Current mass in system = 1.09303e-09 + Linear momentum = (2.02694e-11 -4.62288e-09 0) + |Linear momentum| = 4.62292e-09 + Linear kinetic energy = 1.10609e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 451.286, 540.2 + Mass transfer phase change = 6.13112e-10 + D10, D32, Dmax (mu) = 48.3561, 70.674, 179.911 + Liquid penetration 95% mass (m) = 0.0135338 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0140761, Final residual = 7.72789e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0334293, Final residual = 1.16329e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000605057, Final residual = 4.32505e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000373389, Final residual = 3.01825e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000455977, Final residual = 4.00031e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000455978, Final residual = 4.01141e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000609864, Final residual = 4.11469e-08, No Iterations 1 +min/max(T) = 806.587, 2748.98 +GAMG: Solving for p, Initial residual = 0.0183212, Final residual = 0.000239021, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.93802e-05, global = 1.82376e-05, cumulative = 0.0140243 +GAMG: Solving for p, Initial residual = 0.000240455, Final residual = 9.2695e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.8271e-05, global = 1.82682e-05, cumulative = 0.0140426 +smoothSolver: Solving for epsilon, Initial residual = 0.000828467, Final residual = 1.00897e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000808236, Final residual = 1.49946e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.112003 s +other Time = 0 s +rho Equations = 0.000208 s +U Equations = 0.001309 s +Y Equations = 0.0024577 s +E Equations = 0.000507 s +p Equations = 0.00193 s +calculate parcels = 198.965 s +chemistry correctThermo = 0.002122 s +turbulence correct = 0.000857 s +combustion correct(in Y) = 0.10239 s +percentage of chemistry = 91.4175 % +percentage of rho/U/Y/E = 4.00141 % +========Time details of each equation======= +rhoEqn Time = 0.000335 s +rhoEqn assamble = 0.000267 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001309 s +UEqn assamble = 0.000759 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00055 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001707 s +YEqn assamble = 0.000577 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.2e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000383 s +EEqn assamble = 0.000288 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 282.08 s ClockTime = 283 s +Courant Number mean: 0.00393887 max: 0.0174217 +Time = 0.0021075 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21790 + Current mass in system = 1.09144e-09 + Linear momentum = (2.02409e-11 -4.61572e-09 0) + |Linear momentum| = 4.61576e-09 + Linear kinetic energy = 1.10398e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 451.451, 540.2 + Mass transfer phase change = 6.14705e-10 + D10, D32, Dmax (mu) = 48.3116, 70.6308, 179.744 + Liquid penetration 95% mass (m) = 0.0135411 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0126461, Final residual = 7.18174e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0321536, Final residual = 1.13445e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000602889, Final residual = 4.31323e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000377354, Final residual = 3.10348e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000461209, Final residual = 4.11662e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000461214, Final residual = 4.12834e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.0006163, Final residual = 4.16224e-08, No Iterations 1 +min/max(T) = 806.592, 2749.24 +GAMG: Solving for p, Initial residual = 0.0189041, Final residual = 0.000181555, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.9359e-05, global = 1.82427e-05, cumulative = 0.0140609 +GAMG: Solving for p, Initial residual = 0.000180045, Final residual = 5.00944e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.83563e-05, global = 1.8354e-05, cumulative = 0.0140792 +smoothSolver: Solving for epsilon, Initial residual = 0.000825608, Final residual = 1.01184e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000810017, Final residual = 1.51917e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.098224 s +other Time = 0 s +rho Equations = 0.000199 s +U Equations = 0.001225 s +Y Equations = 0.00221149 s +E Equations = 0.00049 s +p Equations = 0.001907 s +calculate parcels = 199.308 s +chemistry correctThermo = 0.002404 s +turbulence correct = 0.000859 s +combustion correct(in Y) = 0.0887105 s +percentage of chemistry = 90.3145 % +percentage of rho/U/Y/E = 4.20009 % +========Time details of each equation======= +rhoEqn Time = 0.000325 s +rhoEqn assamble = 0.000257 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001225 s +UEqn assamble = 0.000727 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000498 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001573 s +YEqn assamble = 0.000544 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000121 s +YEqn correct boundary = 0 s +EEqn Time = 0.000365 s +EEqn assamble = 0.000272 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 282.53 s ClockTime = 283 s +Courant Number mean: 0.00408331 max: 0.0180047 +Time = 0.00211 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21789 + Current mass in system = 1.08982e-09 + Linear momentum = (2.01548e-11 -4.60848e-09 0) + |Linear momentum| = 4.60852e-09 + Linear kinetic energy = 1.10186e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 451.619, 540.2 + Mass transfer phase change = 6.16322e-10 + D10, D32, Dmax (mu) = 48.2621, 70.5907, 179.576 + Liquid penetration 95% mass (m) = 0.0135495 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0117602, Final residual = 6.6844e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0309992, Final residual = 1.10634e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000604619, Final residual = 4.37232e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000380374, Final residual = 3.19609e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000465858, Final residual = 4.2446e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000465892, Final residual = 4.25666e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000620174, Final residual = 4.17093e-08, No Iterations 1 +min/max(T) = 806.599, 2749.56 +GAMG: Solving for p, Initial residual = 0.0198694, Final residual = 0.000160121, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.94584e-05, global = 1.84815e-05, cumulative = 0.0140977 +GAMG: Solving for p, Initial residual = 0.000160447, Final residual = 2.86657e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.86394e-05, global = 1.86378e-05, cumulative = 0.0141163 +smoothSolver: Solving for epsilon, Initial residual = 0.000818456, Final residual = 1.01376e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000810241, Final residual = 1.53949e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.077584 s +other Time = 0 s +rho Equations = 0.00018 s +U Equations = 0.001229 s +Y Equations = 0.0028645 s +E Equations = 0.000506 s +p Equations = 0.001925 s +calculate parcels = 199.57 s +chemistry correctThermo = 0.001968 s +turbulence correct = 0.000881 s +combustion correct(in Y) = 0.0678355 s +percentage of chemistry = 87.4349 % +percentage of rho/U/Y/E = 6.16042 % +========Time details of each equation======= +rhoEqn Time = 0.000312 s +rhoEqn assamble = 0.000241 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001229 s +UEqn assamble = 0.00078 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000449 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002247 s +YEqn assamble = 0.000938 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000155 s +YEqn correct boundary = 0 s +EEqn Time = 0.00038 s +EEqn assamble = 0.000285 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 282.86 s ClockTime = 283 s +Courant Number mean: 0.00422636 max: 0.0185915 +Time = 0.0021125 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21788 + Current mass in system = 1.08819e-09 + Linear momentum = (2.00662e-11 -4.60124e-09 0) + |Linear momentum| = 4.60128e-09 + Linear kinetic energy = 1.09972e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 451.788, 540.2 + Mass transfer phase change = 6.17956e-10 + D10, D32, Dmax (mu) = 48.1956, 70.5488, 179.407 + Liquid penetration 95% mass (m) = 0.0135565 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.012381, Final residual = 6.99145e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0298739, Final residual = 1.07123e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000612362, Final residual = 4.41754e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000381626, Final residual = 3.27318e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000471197, Final residual = 4.36266e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00047121, Final residual = 4.37509e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000629181, Final residual = 4.25427e-08, No Iterations 1 +min/max(T) = 806.607, 2749.8 +GAMG: Solving for p, Initial residual = 0.0213792, Final residual = 0.00021654, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.97187e-05, global = 1.85904e-05, cumulative = 0.0141349 +GAMG: Solving for p, Initial residual = 0.000217385, Final residual = 8.64742e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.88331e-05, global = 1.88301e-05, cumulative = 0.0141537 +smoothSolver: Solving for epsilon, Initial residual = 0.000815671, Final residual = 1.01532e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000811747, Final residual = 1.56448e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.11618 s +other Time = 0 s +rho Equations = 0.000253 s +U Equations = 0.001778 s +Y Equations = 0.00435561 s +E Equations = 0.001232 s +p Equations = 0.002691 s +calculate parcels = 199.912 s +chemistry correctThermo = 0.00637 s +turbulence correct = 0.000864 s +combustion correct(in Y) = 0.0983294 s +percentage of chemistry = 84.6354 % +percentage of rho/U/Y/E = 6.55759 % +========Time details of each equation======= +rhoEqn Time = 0.0004 s +rhoEqn assamble = 0.000302 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001776 s +UEqn assamble = 0.000996 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00078 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.003284 s +YEqn assamble = 0.001117 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000502 s +YEqn correct boundary = 0 s +EEqn Time = 0.000912 s +EEqn assamble = 0.000645 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000267 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 283.32 s ClockTime = 284 s +Courant Number mean: 0.00436667 max: 0.0191788 +Time = 0.002115 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21787 + Current mass in system = 1.08656e-09 + Linear momentum = (1.99229e-11 -4.59392e-09 0) + |Linear momentum| = 4.59396e-09 + Linear kinetic energy = 1.09755e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 451.957, 540.2 + Mass transfer phase change = 6.19586e-10 + D10, D32, Dmax (mu) = 48.1306, 70.5068, 179.239 + Liquid penetration 95% mass (m) = 0.0135637 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0142513, Final residual = 8.14052e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0289945, Final residual = 1.04508e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000606592, Final residual = 4.36637e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000380945, Final residual = 3.34081e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000471303, Final residual = 4.471e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000471321, Final residual = 4.48421e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000633792, Final residual = 4.30312e-08, No Iterations 1 +min/max(T) = 806.617, 2750 +GAMG: Solving for p, Initial residual = 0.0231136, Final residual = 0.000296082, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.02478e-05, global = 1.86137e-05, cumulative = 0.0141724 +GAMG: Solving for p, Initial residual = 0.000297196, Final residual = 3.21281e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.87967e-05, global = 1.87949e-05, cumulative = 0.0141912 +smoothSolver: Solving for epsilon, Initial residual = 0.000809648, Final residual = 1.01532e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000812973, Final residual = 1.58642e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.117665 s +other Time = 1e-06 s +rho Equations = 0.00018 s +U Equations = 0.001358 s +Y Equations = 0.00361906 s +E Equations = 0.001039 s +p Equations = 0.003761 s +calculate parcels = 200.279 s +chemistry correctThermo = 0.005505 s +turbulence correct = 0.000918 s +combustion correct(in Y) = 0.101059 s +percentage of chemistry = 85.887 % +percentage of rho/U/Y/E = 5.26585 % +========Time details of each equation======= +rhoEqn Time = 0.000392 s +rhoEqn assamble = 0.0003 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001358 s +UEqn assamble = 0.000812 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000546 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002963 s +YEqn assamble = 0.001092 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000568 s +YEqn correct boundary = 0 s +EEqn Time = 0.0008 s +EEqn assamble = 0.000588 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000212 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 283.81 s ClockTime = 284 s +Courant Number mean: 0.00450249 max: 0.0197472 +Time = 0.0021175 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21787 + Current mass in system = 1.08496e-09 + Linear momentum = (1.97423e-11 -4.58651e-09 0) + |Linear momentum| = 4.58655e-09 + Linear kinetic energy = 1.09536e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 452.126, 540.2 + Mass transfer phase change = 6.21178e-10 + D10, D32, Dmax (mu) = 48.0648, 70.4621, 179.242 + Liquid penetration 95% mass (m) = 0.0135706 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0145258, Final residual = 8.3904e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0280954, Final residual = 1.01574e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000587956, Final residual = 4.12286e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000380728, Final residual = 3.3943e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000469963, Final residual = 4.50563e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000469985, Final residual = 4.51872e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000634181, Final residual = 4.25149e-08, No Iterations 1 +min/max(T) = 806.629, 2749.99 +GAMG: Solving for p, Initial residual = 0.0246864, Final residual = 0.000277744, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.94945e-05, global = 1.8253e-05, cumulative = 0.0142094 +GAMG: Solving for p, Initial residual = 0.000279432, Final residual = 2.28703e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.83439e-05, global = 1.83432e-05, cumulative = 0.0142277 +smoothSolver: Solving for epsilon, Initial residual = 0.000804268, Final residual = 1.01186e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000812276, Final residual = 1.60478e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.096992 s +other Time = 1e-06 s +rho Equations = 0.000187 s +U Equations = 0.001209 s +Y Equations = 0.00235148 s +E Equations = 0.00049 s +p Equations = 0.001985 s +calculate parcels = 200.638 s +chemistry correctThermo = 0.002065 s +turbulence correct = 0.00085 s +combustion correct(in Y) = 0.0876525 s +percentage of chemistry = 90.3709 % +percentage of rho/U/Y/E = 4.3689 % +========Time details of each equation======= +rhoEqn Time = 0.000313 s +rhoEqn assamble = 0.000247 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001208 s +UEqn assamble = 0.000717 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000491 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00171 s +YEqn assamble = 0.000641 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000167 s +YEqn correct boundary = 0 s +EEqn Time = 0.000367 s +EEqn assamble = 0.000275 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 284.26 s ClockTime = 285 s +Courant Number mean: 0.004632 max: 0.0203135 +Time = 0.00212 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21786 + Current mass in system = 1.08336e-09 + Linear momentum = (1.95044e-11 -4.57898e-09 0) + |Linear momentum| = 4.57902e-09 + Linear kinetic energy = 1.09312e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 452.298, 540.2 + Mass transfer phase change = 6.22787e-10 + D10, D32, Dmax (mu) = 48.0112, 70.4193, 179.712 + Liquid penetration 95% mass (m) = 0.0135784 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0126834, Final residual = 7.43683e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0270451, Final residual = 9.74998e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000586023, Final residual = 4.08597e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000383874, Final residual = 3.45295e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00047305, Final residual = 4.59326e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000473078, Final residual = 4.6066e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000636213, Final residual = 4.26413e-08, No Iterations 1 +min/max(T) = 806.645, 2750.09 +GAMG: Solving for p, Initial residual = 0.025675, Final residual = 0.000228881, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.965e-05, global = 1.84077e-05, cumulative = 0.0142462 +GAMG: Solving for p, Initial residual = 0.000227372, Final residual = 4.37319e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.85498e-05, global = 1.8548e-05, cumulative = 0.0142647 +smoothSolver: Solving for epsilon, Initial residual = 0.000801693, Final residual = 1.01458e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000814398, Final residual = 1.62544e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.109736 s +other Time = 0 s +rho Equations = 0.000176 s +U Equations = 0.001178 s +Y Equations = 0.00223917 s +E Equations = 0.00061 s +p Equations = 0.002353 s +calculate parcels = 200.98 s +chemistry correctThermo = 0.002911 s +turbulence correct = 0.000987 s +combustion correct(in Y) = 0.0990738 s +percentage of chemistry = 90.2838 % +percentage of rho/U/Y/E = 3.83026 % +========Time details of each equation======= +rhoEqn Time = 0.000326 s +rhoEqn assamble = 0.000258 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001178 s +UEqn assamble = 0.000678 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.0005 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001607 s +YEqn assamble = 0.000572 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000147 s +YEqn correct boundary = 0 s +EEqn Time = 0.000447 s +EEqn assamble = 0.000334 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 284.72 s ClockTime = 285 s +Courant Number mean: 0.00475831 max: 0.0208482 +Time = 0.0021225 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21784 + Current mass in system = 1.08168e-09 + Linear momentum = (1.92312e-11 -4.57137e-09 0) + |Linear momentum| = 4.57141e-09 + Linear kinetic energy = 1.09086e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 452.47, 540.2 + Mass transfer phase change = 6.24461e-10 + D10, D32, Dmax (mu) = 47.9492, 70.3786, 180.181 + Liquid penetration 95% mass (m) = 0.0135858 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0100388, Final residual = 5.93985e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0260387, Final residual = 9.39291e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000611355, Final residual = 4.34624e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000386059, Final residual = 3.50864e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000482113, Final residual = 4.73054e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000482174, Final residual = 4.74416e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000644329, Final residual = 4.34665e-08, No Iterations 1 +min/max(T) = 806.663, 2750.33 +GAMG: Solving for p, Initial residual = 0.0274583, Final residual = 0.000292195, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.0477e-05, global = 1.90391e-05, cumulative = 0.0142837 +GAMG: Solving for p, Initial residual = 0.00029473, Final residual = 1.90571e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.9291e-05, global = 1.92902e-05, cumulative = 0.014303 +smoothSolver: Solving for epsilon, Initial residual = 0.00080034, Final residual = 1.0224e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000817031, Final residual = 1.65516e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.077983 s +other Time = 0 s +rho Equations = 0.000179 s +U Equations = 0.001039 s +Y Equations = 0.0021216 s +E Equations = 0.000483 s +p Equations = 0.002012 s +calculate parcels = 201.31 s +chemistry correctThermo = 0.002147 s +turbulence correct = 0.000834 s +combustion correct(in Y) = 0.0689724 s +percentage of chemistry = 88.4454 % +percentage of rho/U/Y/E = 4.90183 % +========Time details of each equation======= +rhoEqn Time = 0.000302 s +rhoEqn assamble = 0.00024 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001037 s +UEqn assamble = 0.000628 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000409 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001559 s +YEqn assamble = 0.000548 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000128 s +YEqn correct boundary = 0 s +EEqn Time = 0.000365 s +EEqn assamble = 0.000274 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 285.12 s ClockTime = 286 s +Courant Number mean: 0.00488504 max: 0.0213702 +Time = 0.002125 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21784 + Current mass in system = 1.08008e-09 + Linear momentum = (1.89266e-11 -4.56368e-09 0) + |Linear momentum| = 4.56372e-09 + Linear kinetic energy = 1.08857e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 452.641, 540.2 + Mass transfer phase change = 6.26058e-10 + D10, D32, Dmax (mu) = 47.8844, 70.3329, 180.646 + Liquid penetration 95% mass (m) = 0.0135935 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0112054, Final residual = 6.69971e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.025369, Final residual = 9.18074e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000583667, Final residual = 3.97957e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000383396, Final residual = 3.54334e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000476335, Final residual = 4.72495e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000476403, Final residual = 4.73847e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00064412, Final residual = 4.29589e-08, No Iterations 1 +min/max(T) = 806.685, 2750.41 +GAMG: Solving for p, Initial residual = 0.0302505, Final residual = 0.000380546, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.97973e-05, global = 1.83883e-05, cumulative = 0.0143214 +GAMG: Solving for p, Initial residual = 0.000384578, Final residual = 2.5697e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.84078e-05, global = 1.84069e-05, cumulative = 0.0143398 +smoothSolver: Solving for epsilon, Initial residual = 0.000793776, Final residual = 1.01391e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00081378, Final residual = 1.66273e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.111178 s +other Time = 0 s +rho Equations = 0.000179 s +U Equations = 0.001269 s +Y Equations = 0.00252494 s +E Equations = 0.000606 s +p Equations = 0.002475 s +calculate parcels = 201.582 s +chemistry correctThermo = 0.002884 s +turbulence correct = 0.001031 s +combustion correct(in Y) = 0.1 s +percentage of chemistry = 89.9459 % +percentage of rho/U/Y/E = 4.11857 % +========Time details of each equation======= +rhoEqn Time = 0.000328 s +rhoEqn assamble = 0.000258 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001268 s +UEqn assamble = 0.000751 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000517 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001873 s +YEqn assamble = 0.000638 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000227 s +YEqn correct boundary = 0 s +EEqn Time = 0.000445 s +EEqn assamble = 0.000331 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 285.51 s ClockTime = 286 s +Courant Number mean: 0.00500517 max: 0.0218066 +Time = 0.0021275 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21783 + Current mass in system = 1.07848e-09 + Linear momentum = (1.8597e-11 -4.55594e-09 0) + |Linear momentum| = 4.55598e-09 + Linear kinetic energy = 1.08626e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 452.811, 540.2 + Mass transfer phase change = 6.27662e-10 + D10, D32, Dmax (mu) = 47.8466, 70.2869, 181.106 + Liquid penetration 95% mass (m) = 0.0136009 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0095536, Final residual = 5.3754e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0243922, Final residual = 8.77417e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000582995, Final residual = 3.9664e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000385556, Final residual = 3.56917e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000479805, Final residual = 4.77644e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000479856, Final residual = 4.79008e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000648481, Final residual = 4.31583e-08, No Iterations 1 +min/max(T) = 806.712, 2750.52 +GAMG: Solving for p, Initial residual = 0.0314696, Final residual = 0.000244984, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.94447e-05, global = 1.84166e-05, cumulative = 0.0143582 +GAMG: Solving for p, Initial residual = 0.000247138, Final residual = 5.05543e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.84949e-05, global = 1.84929e-05, cumulative = 0.0143767 +smoothSolver: Solving for epsilon, Initial residual = 0.000796839, Final residual = 1.02218e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000817103, Final residual = 1.68427e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102696 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001079 s +Y Equations = 0.0023866 s +E Equations = 0.000629 s +p Equations = 0.002353 s +calculate parcels = 201.915 s +chemistry correctThermo = 0.002857 s +turbulence correct = 0.00109 s +combustion correct(in Y) = 0.0919374 s +percentage of chemistry = 89.5238 % +percentage of rho/U/Y/E = 4.15946 % +========Time details of each equation======= +rhoEqn Time = 0.000329 s +rhoEqn assamble = 0.000259 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001079 s +UEqn assamble = 0.000664 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000415 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001839 s +YEqn assamble = 0.00064 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000225 s +YEqn correct boundary = 0 s +EEqn Time = 0.000471 s +EEqn assamble = 0.000352 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000119 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 285.94 s ClockTime = 287 s +Courant Number mean: 0.00512035 max: 0.0221765 +Time = 0.00213 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21781 + Current mass in system = 1.07686e-09 + Linear momentum = (1.82554e-11 -4.54816e-09 0) + |Linear momentum| = 4.5482e-09 + Linear kinetic energy = 1.08395e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 452.981, 540.2 + Mass transfer phase change = 6.29283e-10 + D10, D32, Dmax (mu) = 47.8107, 70.2432, 181.559 + Liquid penetration 95% mass (m) = 0.0136092 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00798124, Final residual = 3.83906e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.023509, Final residual = 8.44788e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000579814, Final residual = 4.02003e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00038753, Final residual = 3.59741e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000481794, Final residual = 4.82756e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000481847, Final residual = 4.84146e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000648218, Final residual = 4.32391e-08, No Iterations 1 +min/max(T) = 806.742, 2750.69 +GAMG: Solving for p, Initial residual = 0.0330717, Final residual = 0.000195599, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.93912e-05, global = 1.85841e-05, cumulative = 0.0143953 +GAMG: Solving for p, Initial residual = 0.00019303, Final residual = 4.42472e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.86861e-05, global = 1.86847e-05, cumulative = 0.014414 +smoothSolver: Solving for epsilon, Initial residual = 0.000796037, Final residual = 1.02628e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000818265, Final residual = 1.70212e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103214 s +other Time = 0 s +rho Equations = 0.000179 s +U Equations = 0.001264 s +Y Equations = 0.00231759 s +E Equations = 0.000516 s +p Equations = 0.001765 s +calculate parcels = 202.244 s +chemistry correctThermo = 0.002054 s +turbulence correct = 0.000854 s +combustion correct(in Y) = 0.0940624 s +percentage of chemistry = 91.1334 % +percentage of rho/U/Y/E = 4.14342 % +========Time details of each equation======= +rhoEqn Time = 0.000294 s +rhoEqn assamble = 0.000232 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001264 s +UEqn assamble = 0.000762 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000502 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001677 s +YEqn assamble = 0.000584 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000155 s +YEqn correct boundary = 0 s +EEqn Time = 0.000395 s +EEqn assamble = 0.000298 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.7e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 286.38 s ClockTime = 287 s +Courant Number mean: 0.00523104 max: 0.0224864 +Time = 0.0021325 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21777 + Current mass in system = 1.07521e-09 + Linear momentum = (1.79266e-11 -4.5404e-09 0) + |Linear momentum| = 4.54044e-09 + Linear kinetic energy = 1.08163e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 453.152, 540.2 + Mass transfer phase change = 6.30934e-10 + D10, D32, Dmax (mu) = 47.7968, 70.2009, 182.004 + Liquid penetration 95% mass (m) = 0.0136168 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00705887, Final residual = 3.12552e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0225669, Final residual = 8.11312e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000592456, Final residual = 4.11303e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000387956, Final residual = 3.62756e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000486413, Final residual = 4.88948e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000486468, Final residual = 4.90346e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000652502, Final residual = 4.35449e-08, No Iterations 1 +min/max(T) = 806.778, 2750.86 +GAMG: Solving for p, Initial residual = 0.0358049, Final residual = 0.000237492, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.96884e-05, global = 1.88821e-05, cumulative = 0.0144329 +GAMG: Solving for p, Initial residual = 0.000241443, Final residual = 6.50062e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.90231e-05, global = 1.90217e-05, cumulative = 0.0144519 +smoothSolver: Solving for epsilon, Initial residual = 0.000796093, Final residual = 1.0353e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000819322, Final residual = 1.72159e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100496 s +other Time = 0 s +rho Equations = 0.000195 s +U Equations = 0.001322 s +Y Equations = 0.00242016 s +E Equations = 0.000588 s +p Equations = 0.001847 s +calculate parcels = 202.572 s +chemistry correctThermo = 0.002393 s +turbulence correct = 0.00084 s +combustion correct(in Y) = 0.0906688 s +percentage of chemistry = 90.2213 % +percentage of rho/U/Y/E = 4.50283 % +========Time details of each equation======= +rhoEqn Time = 0.000329 s +rhoEqn assamble = 0.000253 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001322 s +UEqn assamble = 0.000809 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000513 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001769 s +YEqn assamble = 0.000639 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000185 s +YEqn correct boundary = 0 s +EEqn Time = 0.000436 s +EEqn assamble = 0.000326 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00011 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 286.8 s ClockTime = 287 s +Courant Number mean: 0.00533815 max: 0.0227557 +Time = 0.002135 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21776 + Current mass in system = 1.07359e-09 + Linear momentum = (1.75846e-11 -4.53267e-09 0) + |Linear momentum| = 4.53271e-09 + Linear kinetic energy = 1.07934e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 453.322, 540.2 + Mass transfer phase change = 6.3255e-10 + D10, D32, Dmax (mu) = 47.7428, 70.156, 182.439 + Liquid penetration 95% mass (m) = 0.0136244 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00766552, Final residual = 3.62936e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0216518, Final residual = 7.79407e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0005791, Final residual = 4.00227e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000386724, Final residual = 3.6627e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000483114, Final residual = 4.9163e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000483175, Final residual = 4.93033e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000653234, Final residual = 4.36716e-08, No Iterations 1 +min/max(T) = 806.818, 2750.94 +GAMG: Solving for p, Initial residual = 0.0390855, Final residual = 0.000318873, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.96303e-05, global = 1.85752e-05, cumulative = 0.0144705 +GAMG: Solving for p, Initial residual = 0.000323365, Final residual = 2.49276e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.86248e-05, global = 1.86239e-05, cumulative = 0.0144891 +smoothSolver: Solving for epsilon, Initial residual = 0.000792365, Final residual = 1.03768e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000817932, Final residual = 1.72949e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.091321 s +other Time = 0 s +rho Equations = 0.000166 s +U Equations = 0.001003 s +Y Equations = 0.00239848 s +E Equations = 0.000596 s +p Equations = 0.002452 s +calculate parcels = 202.935 s +chemistry correctThermo = 0.002914 s +turbulence correct = 0.00098 s +combustion correct(in Y) = 0.0806165 s +percentage of chemistry = 88.2782 % +percentage of rho/U/Y/E = 4.55916 % +========Time details of each equation======= +rhoEqn Time = 0.000309 s +rhoEqn assamble = 0.000241 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001001 s +UEqn assamble = 0.000582 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000419 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001845 s +YEqn assamble = 0.000635 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000229 s +YEqn correct boundary = 0 s +EEqn Time = 0.000441 s +EEqn assamble = 0.000329 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 287.26 s ClockTime = 288 s +Courant Number mean: 0.00543709 max: 0.0229401 +Time = 0.0021375 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21775 + Current mass in system = 1.07197e-09 + Linear momentum = (1.72271e-11 -4.52497e-09 0) + |Linear momentum| = 4.52501e-09 + Linear kinetic energy = 1.07705e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 453.491, 540.2 + Mass transfer phase change = 6.34171e-10 + D10, D32, Dmax (mu) = 47.6935, 70.1119, 182.86 + Liquid penetration 95% mass (m) = 0.0136323 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00652672, Final residual = 2.86481e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0206083, Final residual = 7.40919e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000578641, Final residual = 4.02828e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000387695, Final residual = 3.69912e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00048479, Final residual = 4.96087e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00048484, Final residual = 4.97493e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000655638, Final residual = 4.37967e-08, No Iterations 1 +min/max(T) = 806.863, 2750.92 +GAMG: Solving for p, Initial residual = 0.041588, Final residual = 0.000234128, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.93459e-05, global = 1.86193e-05, cumulative = 0.0145077 +GAMG: Solving for p, Initial residual = 0.000237401, Final residual = 7.52509e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.86839e-05, global = 1.86819e-05, cumulative = 0.0145264 +smoothSolver: Solving for epsilon, Initial residual = 0.000793316, Final residual = 1.04511e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000819569, Final residual = 1.7429e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.083344 s +other Time = 1e-06 s +rho Equations = 0.000166 s +U Equations = 0.001079 s +Y Equations = 0.00220468 s +E Equations = 0.000485 s +p Equations = 0.001843 s +calculate parcels = 203.229 s +chemistry correctThermo = 0.001981 s +turbulence correct = 0.000852 s +combustion correct(in Y) = 0.0745503 s +percentage of chemistry = 89.4489 % +percentage of rho/U/Y/E = 4.72101 % +========Time details of each equation======= +rhoEqn Time = 0.000293 s +rhoEqn assamble = 0.000232 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001079 s +UEqn assamble = 0.000655 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000424 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001602 s +YEqn assamble = 0.000571 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000132 s +YEqn correct boundary = 0 s +EEqn Time = 0.000361 s +EEqn assamble = 0.000271 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 287.64 s ClockTime = 288 s +Courant Number mean: 0.00552846 max: 0.0230329 +Time = 0.00214 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21774 + Current mass in system = 1.07036e-09 + Linear momentum = (1.68491e-11 -4.51733e-09 0) + |Linear momentum| = 4.51736e-09 + Linear kinetic energy = 1.07478e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 453.659, 540.2 + Mass transfer phase change = 6.35782e-10 + D10, D32, Dmax (mu) = 47.6391, 70.0658, 182.924 + Liquid penetration 95% mass (m) = 0.0136398 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00576125, Final residual = 2.60181e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0195166, Final residual = 7.00912e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00057712, Final residual = 4.00538e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00038832, Final residual = 3.73661e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000487232, Final residual = 4.99937e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000487307, Final residual = 5.01344e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00065623, Final residual = 4.38582e-08, No Iterations 1 +min/max(T) = 806.914, 2750.86 +GAMG: Solving for p, Initial residual = 0.0446908, Final residual = 0.000220585, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.92096e-05, global = 1.84994e-05, cumulative = 0.0145449 +GAMG: Solving for p, Initial residual = 0.000221109, Final residual = 7.46353e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.85739e-05, global = 1.85723e-05, cumulative = 0.0145635 +smoothSolver: Solving for epsilon, Initial residual = 0.000794134, Final residual = 1.04751e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000819068, Final residual = 1.74893e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.111931 s +other Time = 1e-06 s +rho Equations = 0.000182 s +U Equations = 0.001254 s +Y Equations = 0.00249843 s +E Equations = 0.000648 s +p Equations = 0.002311 s +calculate parcels = 203.528 s +chemistry correctThermo = 0.002894 s +turbulence correct = 0.001118 s +combustion correct(in Y) = 0.100818 s +percentage of chemistry = 90.0712 % +percentage of rho/U/Y/E = 4.09397 % +========Time details of each equation======= +rhoEqn Time = 0.000329 s +rhoEqn assamble = 0.00026 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001253 s +UEqn assamble = 0.000728 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000525 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001841 s +YEqn assamble = 0.000639 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000194 s +YEqn correct boundary = 0 s +EEqn Time = 0.00048 s +EEqn assamble = 0.000362 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 288.05 s ClockTime = 289 s +Courant Number mean: 0.00561237 max: 0.0230581 +Time = 0.0021425 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21772 + Current mass in system = 1.0687e-09 + Linear momentum = (1.64993e-11 -4.50964e-09 0) + |Linear momentum| = 4.50967e-09 + Linear kinetic energy = 1.07252e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 453.826, 540.2 + Mass transfer phase change = 6.3744e-10 + D10, D32, Dmax (mu) = 47.5958, 70.026, 182.775 + Liquid penetration 95% mass (m) = 0.0136474 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00570368, Final residual = 2.32867e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0183495, Final residual = 6.57075e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000587036, Final residual = 4.30917e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000388854, Final residual = 3.77343e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000490097, Final residual = 5.09552e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00049018, Final residual = 5.10993e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000655564, Final residual = 4.44448e-08, No Iterations 1 +min/max(T) = 806.969, 2750.84 +GAMG: Solving for p, Initial residual = 0.0488143, Final residual = 0.000320082, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.96725e-05, global = 1.89556e-05, cumulative = 0.0145824 +GAMG: Solving for p, Initial residual = 0.000323787, Final residual = 3.90687e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.91074e-05, global = 1.91067e-05, cumulative = 0.0146015 +smoothSolver: Solving for epsilon, Initial residual = 0.000794737, Final residual = 1.05533e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000820096, Final residual = 1.75824e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102162 s +other Time = 0 s +rho Equations = 0.000275 s +U Equations = 0.0014 s +Y Equations = 0.00256105 s +E Equations = 0.000601 s +p Equations = 0.002473 s +calculate parcels = 203.881 s +chemistry correctThermo = 0.002856 s +turbulence correct = 0.001014 s +combustion correct(in Y) = 0.0907259 s +percentage of chemistry = 88.806 % +percentage of rho/U/Y/E = 4.73469 % +========Time details of each equation======= +rhoEqn Time = 0.000423 s +rhoEqn assamble = 0.00033 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001398 s +UEqn assamble = 0.000891 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000507 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001927 s +YEqn assamble = 0.000708 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000196 s +YEqn correct boundary = 0 s +EEqn Time = 0.000441 s +EEqn assamble = 0.000328 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 288.5 s ClockTime = 289 s +Courant Number mean: 0.00569224 max: 0.0230186 +Time = 0.002145 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21771 + Current mass in system = 1.06706e-09 + Linear momentum = (1.61915e-11 -4.50211e-09 0) + |Linear momentum| = 4.50214e-09 + Linear kinetic energy = 1.07029e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 453.992, 540.2 + Mass transfer phase change = 6.39085e-10 + D10, D32, Dmax (mu) = 47.5304, 69.9822, 182.626 + Liquid penetration 95% mass (m) = 0.013656 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00766904, Final residual = 3.46235e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0172415, Final residual = 6.18382e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000588121, Final residual = 4.22086e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000387819, Final residual = 3.80244e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000491539, Final residual = 5.10308e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000491619, Final residual = 5.11732e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000657851, Final residual = 4.42756e-08, No Iterations 1 +min/max(T) = 807.03, 2750.84 +GAMG: Solving for p, Initial residual = 0.0545826, Final residual = 0.000323229, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.94976e-05, global = 1.8873e-05, cumulative = 0.0146204 +GAMG: Solving for p, Initial residual = 0.000336431, Final residual = 9.38781e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.89662e-05, global = 1.89646e-05, cumulative = 0.0146394 +smoothSolver: Solving for epsilon, Initial residual = 0.000794219, Final residual = 1.05513e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00081538, Final residual = 1.75382e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.108963 s +other Time = 0 s +rho Equations = 0.000176 s +U Equations = 0.001172 s +Y Equations = 0.00247351 s +E Equations = 0.0006 s +p Equations = 0.002248 s +calculate parcels = 204.223 s +chemistry correctThermo = 0.00288 s +turbulence correct = 0.001023 s +combustion correct(in Y) = 0.0981855 s +percentage of chemistry = 90.109 % +percentage of rho/U/Y/E = 4.05781 % +========Time details of each equation======= +rhoEqn Time = 0.00032 s +rhoEqn assamble = 0.000252 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001172 s +UEqn assamble = 0.000676 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000496 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001838 s +YEqn assamble = 0.000647 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000193 s +YEqn correct boundary = 0 s +EEqn Time = 0.000441 s +EEqn assamble = 0.000327 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 288.95 s ClockTime = 290 s +Courant Number mean: 0.00576499 max: 0.0229071 +Time = 0.0021475 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21770 + Current mass in system = 1.06546e-09 + Linear momentum = (1.58877e-11 -4.49463e-09 0) + |Linear momentum| = 4.49466e-09 + Linear kinetic energy = 1.06808e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 454.157, 540.2 + Mass transfer phase change = 6.40682e-10 + D10, D32, Dmax (mu) = 47.4891, 69.9365, 182.478 + Liquid penetration 95% mass (m) = 0.013663 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00781671, Final residual = 3.58402e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0159341, Final residual = 5.68116e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000570292, Final residual = 4.05422e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000386571, Final residual = 3.83265e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000488486, Final residual = 5.10017e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000488597, Final residual = 5.11453e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000656992, Final residual = 4.41225e-08, No Iterations 1 +min/max(T) = 807.095, 2750.75 +GAMG: Solving for p, Initial residual = 0.0601372, Final residual = 0.000475564, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.95442e-05, global = 1.83802e-05, cumulative = 0.0146578 +GAMG: Solving for p, Initial residual = 0.000496299, Final residual = 4.71991e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.8403e-05, global = 1.84019e-05, cumulative = 0.0146762 +smoothSolver: Solving for epsilon, Initial residual = 0.000791285, Final residual = 1.05288e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000812234, Final residual = 1.74713e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.108376 s +other Time = 0 s +rho Equations = 0.000185 s +U Equations = 0.001197 s +Y Equations = 0.00246456 s +E Equations = 0.000595 s +p Equations = 0.002709 s +calculate parcels = 204.571 s +chemistry correctThermo = 0.002839 s +turbulence correct = 0.00114 s +combustion correct(in Y) = 0.0969704 s +percentage of chemistry = 89.4759 % +percentage of rho/U/Y/E = 4.09829 % +========Time details of each equation======= +rhoEqn Time = 0.00037 s +rhoEqn assamble = 0.00029 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001196 s +UEqn assamble = 0.00069 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000506 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001814 s +YEqn assamble = 0.000652 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000194 s +YEqn correct boundary = 0 s +EEqn Time = 0.00044 s +EEqn assamble = 0.000328 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 289.41 s ClockTime = 290 s +Courant Number mean: 0.00582694 max: 0.0227452 +Time = 0.00215 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21769 + Current mass in system = 1.06385e-09 + Linear momentum = (1.55791e-11 -4.48719e-09 0) + |Linear momentum| = 4.48722e-09 + Linear kinetic energy = 1.06589e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 454.321, 540.2 + Mass transfer phase change = 6.42289e-10 + D10, D32, Dmax (mu) = 47.4329, 69.8929, 182.33 + Liquid penetration 95% mass (m) = 0.0136713 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00775529, Final residual = 3.6064e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0145836, Final residual = 5.1439e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000565327, Final residual = 4.10001e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000388196, Final residual = 3.86107e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000490106, Final residual = 5.12597e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000490203, Final residual = 5.14045e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000653834, Final residual = 4.40661e-08, No Iterations 1 +min/max(T) = 807.165, 2750.61 +GAMG: Solving for p, Initial residual = 0.0658526, Final residual = 0.000428543, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.93214e-05, global = 1.84767e-05, cumulative = 0.0146946 +GAMG: Solving for p, Initial residual = 0.000448868, Final residual = 3.29565e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.85271e-05, global = 1.85265e-05, cumulative = 0.0147132 +smoothSolver: Solving for epsilon, Initial residual = 0.000790785, Final residual = 1.05623e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000810802, Final residual = 1.74498e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.123693 s +other Time = 1e-06 s +rho Equations = 0.000204 s +U Equations = 0.001386 s +Y Equations = 0.00318462 s +E Equations = 0.000737 s +p Equations = 0.003295 s +calculate parcels = 204.946 s +chemistry correctThermo = 0.003104 s +turbulence correct = 0.001313 s +combustion correct(in Y) = 0.110221 s +percentage of chemistry = 89.1088 % +percentage of rho/U/Y/E = 4.45588 % +========Time details of each equation======= +rhoEqn Time = 0.000391 s +rhoEqn assamble = 0.000309 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001385 s +UEqn assamble = 0.000841 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000544 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002425 s +YEqn assamble = 0.000826 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000273 s +YEqn correct boundary = 0 s +EEqn Time = 0.000544 s +EEqn assamble = 0.000404 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00014 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 289.91 s ClockTime = 290 s +Courant Number mean: 0.00588159 max: 0.0225364 +Time = 0.0021525 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21769 + Current mass in system = 1.06226e-09 + Linear momentum = (1.52727e-11 -4.47981e-09 0) + |Linear momentum| = 4.47983e-09 + Linear kinetic energy = 1.06371e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 454.485, 540.2 + Mass transfer phase change = 6.43881e-10 + D10, D32, Dmax (mu) = 47.364, 69.8473, 182.183 + Liquid penetration 95% mass (m) = 0.0136785 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00703658, Final residual = 3.34744e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0134202, Final residual = 4.76505e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000564305, Final residual = 4.10209e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000389881, Final residual = 3.90485e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000494402, Final residual = 5.16705e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000494487, Final residual = 5.18156e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00065192, Final residual = 4.40498e-08, No Iterations 1 +min/max(T) = 807.24, 2750.47 +GAMG: Solving for p, Initial residual = 0.0736437, Final residual = 0.000451223, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.91547e-05, global = 1.82872e-05, cumulative = 0.0147315 +GAMG: Solving for p, Initial residual = 0.000475129, Final residual = 3.47381e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.83457e-05, global = 1.83454e-05, cumulative = 0.0147498 +smoothSolver: Solving for epsilon, Initial residual = 0.00078755, Final residual = 1.05378e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000808061, Final residual = 1.73711e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.078537 s +other Time = 0 s +rho Equations = 0.00018 s +U Equations = 0.001092 s +Y Equations = 0.0022356 s +E Equations = 0.000516 s +p Equations = 0.002323 s +calculate parcels = 205.205 s +chemistry correctThermo = 0.002023 s +turbulence correct = 0.000897 s +combustion correct(in Y) = 0.0690154 s +percentage of chemistry = 87.8763 % +percentage of rho/U/Y/E = 5.12319 % +========Time details of each equation======= +rhoEqn Time = 0.000354 s +rhoEqn assamble = 0.00028 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001091 s +UEqn assamble = 0.000667 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000424 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001633 s +YEqn assamble = 0.000546 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00013 s +YEqn correct boundary = 0 s +EEqn Time = 0.000391 s +EEqn assamble = 0.000293 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.8e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 290.25 s ClockTime = 291 s +Courant Number mean: 0.00592973 max: 0.0223454 +Time = 0.002155 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21765 + Current mass in system = 1.06064e-09 + Linear momentum = (1.49708e-11 -4.47237e-09 0) + |Linear momentum| = 4.4724e-09 + Linear kinetic energy = 1.06153e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 454.649, 540.2 + Mass transfer phase change = 6.45506e-10 + D10, D32, Dmax (mu) = 47.3483, 69.8096, 182.035 + Liquid penetration 95% mass (m) = 0.013687 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00628629, Final residual = 2.84977e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0125679, Final residual = 4.55086e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000559145, Final residual = 4.19329e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000391452, Final residual = 3.95613e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000493715, Final residual = 5.22045e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000493809, Final residual = 5.23534e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000648147, Final residual = 4.40996e-08, No Iterations 1 +min/max(T) = 807.319, 2750.41 +GAMG: Solving for p, Initial residual = 0.0841806, Final residual = 0.000526259, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.94245e-05, global = 1.8631e-05, cumulative = 0.0147684 +GAMG: Solving for p, Initial residual = 0.000565153, Final residual = 2.79083e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.87365e-05, global = 1.87362e-05, cumulative = 0.0147872 +smoothSolver: Solving for epsilon, Initial residual = 0.000785662, Final residual = 1.05583e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000806438, Final residual = 1.73596e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.113265 s +other Time = 0 s +rho Equations = 0.000185 s +U Equations = 0.001227 s +Y Equations = 0.00209559 s +E Equations = 0.000479 s +p Equations = 0.002388 s +calculate parcels = 205.533 s +chemistry correctThermo = 0.002117 s +turbulence correct = 0.000999 s +combustion correct(in Y) = 0.103567 s +percentage of chemistry = 91.4381 % +percentage of rho/U/Y/E = 3.5197 % +========Time details of each equation======= +rhoEqn Time = 0.000329 s +rhoEqn assamble = 0.000256 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001227 s +UEqn assamble = 0.000739 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000488 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001448 s +YEqn assamble = 0.000525 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.6e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000361 s +EEqn assamble = 0.00027 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 290.69 s ClockTime = 291 s +Courant Number mean: 0.00597349 max: 0.0221564 +Time = 0.0021575 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21765 + Current mass in system = 1.05905e-09 + Linear momentum = (1.46792e-11 -4.46502e-09 0) + |Linear momentum| = 4.46504e-09 + Linear kinetic energy = 1.05936e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 454.813, 540.2 + Mass transfer phase change = 6.47095e-10 + D10, D32, Dmax (mu) = 47.2797, 69.7637, 181.886 + Liquid penetration 95% mass (m) = 0.0136943 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00661635, Final residual = 3.23962e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0119066, Final residual = 4.40033e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000561603, Final residual = 4.1533e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00039178, Final residual = 4.00014e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000498584, Final residual = 5.27452e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000498665, Final residual = 5.28926e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000648974, Final residual = 4.40108e-08, No Iterations 1 +min/max(T) = 807.401, 2750.36 +GAMG: Solving for p, Initial residual = 0.0990961, Final residual = 0.000578061, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.90925e-05, global = 1.8246e-05, cumulative = 0.0148054 +GAMG: Solving for p, Initial residual = 0.000633825, Final residual = 2.19803e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.83099e-05, global = 1.83096e-05, cumulative = 0.0148237 +smoothSolver: Solving for epsilon, Initial residual = 0.000781846, Final residual = 1.04822e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000803445, Final residual = 1.72743e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.106673 s +other Time = 0 s +rho Equations = 0.000157 s +U Equations = 0.00099 s +Y Equations = 0.0024431 s +E Equations = 0.00059 s +p Equations = 0.00257 s +calculate parcels = 205.887 s +chemistry correctThermo = 0.002904 s +turbulence correct = 0.001027 s +combustion correct(in Y) = 0.0958009 s +percentage of chemistry = 89.808 % +percentage of rho/U/Y/E = 3.91861 % +========Time details of each equation======= +rhoEqn Time = 0.000313 s +rhoEqn assamble = 0.000245 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000988 s +UEqn assamble = 0.000577 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000411 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001899 s +YEqn assamble = 0.000655 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000241 s +YEqn correct boundary = 0 s +EEqn Time = 0.000435 s +EEqn assamble = 0.000324 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 291.15 s ClockTime = 292 s +Courant Number mean: 0.0060085 max: 0.0220353 +Time = 0.00216 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21765 + Current mass in system = 1.05746e-09 + Linear momentum = (1.43971e-11 -4.45765e-09 0) + |Linear momentum| = 4.45767e-09 + Linear kinetic energy = 1.05719e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 454.977, 540.2 + Mass transfer phase change = 6.48683e-10 + D10, D32, Dmax (mu) = 47.2113, 69.718, 181.738 + Liquid penetration 95% mass (m) = 0.0137025 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00645905, Final residual = 3.48941e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0112289, Final residual = 4.23826e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000558747, Final residual = 4.16292e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00039279, Final residual = 4.0374e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000500585, Final residual = 5.31614e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000500669, Final residual = 5.33097e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000646192, Final residual = 4.39169e-08, No Iterations 1 +min/max(T) = 807.487, 2750.28 +GAMG: Solving for p, Initial residual = 0.117817, Final residual = 0.000566904, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.89692e-05, global = 1.82183e-05, cumulative = 0.0148419 +GAMG: Solving for p, Initial residual = 0.00064704, Final residual = 8.79148e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.83103e-05, global = 1.83094e-05, cumulative = 0.0148603 +smoothSolver: Solving for epsilon, Initial residual = 0.000778368, Final residual = 1.04255e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000800681, Final residual = 1.72227e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.111138 s +other Time = 0 s +rho Equations = 0.000198 s +U Equations = 0.001346 s +Y Equations = 0.00249705 s +E Equations = 0.000637 s +p Equations = 0.002227 s +calculate parcels = 206.234 s +chemistry correctThermo = 0.00288 s +turbulence correct = 0.001023 s +combustion correct(in Y) = 0.100117 s +percentage of chemistry = 90.0835 % +percentage of rho/U/Y/E = 4.20923 % +========Time details of each equation======= +rhoEqn Time = 0.000335 s +rhoEqn assamble = 0.000261 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001343 s +UEqn assamble = 0.000809 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000534 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001838 s +YEqn assamble = 0.000641 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000187 s +YEqn correct boundary = 0 s +EEqn Time = 0.000457 s +EEqn assamble = 0.000339 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 291.61 s ClockTime = 292 s +Courant Number mean: 0.00603488 max: 0.0220035 +Time = 0.0021625 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21765 + Current mass in system = 1.05587e-09 + Linear momentum = (1.41273e-11 -4.45023e-09 0) + |Linear momentum| = 4.45026e-09 + Linear kinetic energy = 1.05499e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 455.141, 540.2 + Mass transfer phase change = 6.50271e-10 + D10, D32, Dmax (mu) = 47.1436, 69.6723, 181.584 + Liquid penetration 95% mass (m) = 0.0137107 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00595525, Final residual = 3.47421e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.010571, Final residual = 4.09201e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000556155, Final residual = 4.15994e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000393284, Final residual = 4.06215e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000501761, Final residual = 5.34209e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00050184, Final residual = 5.35697e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000641968, Final residual = 4.37221e-08, No Iterations 1 +min/max(T) = 807.575, 2750.2 +GAMG: Solving for p, Initial residual = 0.143639, Final residual = 0.000632209, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.89057e-05, global = 1.82039e-05, cumulative = 0.0148785 +GAMG: Solving for p, Initial residual = 0.000687889, Final residual = 8.27286e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.83014e-05, global = 1.83006e-05, cumulative = 0.0148968 +smoothSolver: Solving for epsilon, Initial residual = 0.000772674, Final residual = 1.03509e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000796717, Final residual = 1.71483e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.105063 s +other Time = 1e-06 s +rho Equations = 0.000142 s +U Equations = 0.001084 s +Y Equations = 0.00237756 s +E Equations = 0.000598 s +p Equations = 0.002227 s +calculate parcels = 206.571 s +chemistry correctThermo = 0.002883 s +turbulence correct = 0.000984 s +combustion correct(in Y) = 0.0945934 s +percentage of chemistry = 90.035 % +percentage of rho/U/Y/E = 3.99908 % +========Time details of each equation======= +rhoEqn Time = 0.000287 s +rhoEqn assamble = 0.000228 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001083 s +UEqn assamble = 0.000666 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000417 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001835 s +YEqn assamble = 0.000634 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000236 s +YEqn correct boundary = 0 s +EEqn Time = 0.000443 s +EEqn assamble = 0.000329 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 292.05 s ClockTime = 293 s +Courant Number mean: 0.00605253 max: 0.0219577 +Time = 0.002165 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21763 + Current mass in system = 1.05428e-09 + Linear momentum = (1.38729e-11 -4.44275e-09 0) + |Linear momentum| = 4.44277e-09 + Linear kinetic energy = 1.05277e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 455.304, 540.2 + Mass transfer phase change = 6.5186e-10 + D10, D32, Dmax (mu) = 47.1227, 69.6281, 181.423 + Liquid penetration 95% mass (m) = 0.0137182 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00604685, Final residual = 3.50308e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00992842, Final residual = 3.95041e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000552995, Final residual = 4.13255e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000393622, Final residual = 4.07321e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000502486, Final residual = 5.34798e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000502567, Final residual = 5.36286e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000637437, Final residual = 4.32749e-08, No Iterations 1 +min/max(T) = 807.666, 2750.14 +GAMG: Solving for p, Initial residual = 0.162996, Final residual = 0.000661018, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.88615e-05, global = 1.82123e-05, cumulative = 0.014915 +GAMG: Solving for p, Initial residual = 0.000692428, Final residual = 9.86044e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.83118e-05, global = 1.83112e-05, cumulative = 0.0149333 +smoothSolver: Solving for epsilon, Initial residual = 0.000765839, Final residual = 1.02578e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000792012, Final residual = 1.70346e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.07872 s +other Time = 0 s +rho Equations = 0.000182 s +U Equations = 0.001222 s +Y Equations = 0.00216563 s +E Equations = 0.000528 s +p Equations = 0.002028 s +calculate parcels = 206.909 s +chemistry correctThermo = 0.002042 s +turbulence correct = 0.000862 s +combustion correct(in Y) = 0.0694914 s +percentage of chemistry = 88.2766 % +percentage of rho/U/Y/E = 5.20532 % +========Time details of each equation======= +rhoEqn Time = 0.000321 s +rhoEqn assamble = 0.000258 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001221 s +UEqn assamble = 0.000767 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000454 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001574 s +YEqn assamble = 0.00057 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000115 s +YEqn correct boundary = 0 s +EEqn Time = 0.000403 s +EEqn assamble = 0.000311 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 292.47 s ClockTime = 293 s +Courant Number mean: 0.0060616 max: 0.0218683 +Time = 0.0021675 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21762 + Current mass in system = 1.0527e-09 + Linear momentum = (1.36357e-11 -4.43518e-09 0) + |Linear momentum| = 4.4352e-09 + Linear kinetic energy = 1.05053e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 455.468, 540.2 + Mass transfer phase change = 6.53447e-10 + D10, D32, Dmax (mu) = 47.0761, 69.5831, 181.262 + Liquid penetration 95% mass (m) = 0.0137266 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00626697, Final residual = 3.36603e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00923617, Final residual = 3.79983e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000549185, Final residual = 4.09762e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000393027, Final residual = 4.07318e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000502358, Final residual = 5.34187e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000502433, Final residual = 5.35672e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000632733, Final residual = 4.28387e-08, No Iterations 1 +min/max(T) = 807.758, 2750.07 +GAMG: Solving for p, Initial residual = 0.17508, Final residual = 0.000687935, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.88397e-05, global = 1.81766e-05, cumulative = 0.0149515 +GAMG: Solving for p, Initial residual = 0.000711543, Final residual = 6.47812e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.82909e-05, global = 1.82904e-05, cumulative = 0.0149697 +smoothSolver: Solving for epsilon, Initial residual = 0.000758615, Final residual = 1.01437e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000786383, Final residual = 1.688e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.11033 s +other Time = 1e-06 s +rho Equations = 0.000174 s +U Equations = 0.001148 s +Y Equations = 0.00246185 s +E Equations = 0.000635 s +p Equations = 0.002216 s +calculate parcels = 207.183 s +chemistry correctThermo = 0.00288 s +turbulence correct = 0.000997 s +combustion correct(in Y) = 0.0996141 s +percentage of chemistry = 90.2875 % +percentage of rho/U/Y/E = 4.00512 % +========Time details of each equation======= +rhoEqn Time = 0.000321 s +rhoEqn assamble = 0.000253 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001146 s +UEqn assamble = 0.000646 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.0005 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001818 s +YEqn assamble = 0.000624 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000188 s +YEqn correct boundary = 0 s +EEqn Time = 0.000466 s +EEqn assamble = 0.000346 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00012 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 292.85 s ClockTime = 293 s +Courant Number mean: 0.00606157 max: 0.0217366 +Time = 0.00217 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21761 + Current mass in system = 1.05111e-09 + Linear momentum = (1.34185e-11 -4.42752e-09 0) + |Linear momentum| = 4.42754e-09 + Linear kinetic energy = 1.04824e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 455.632, 540.2 + Mass transfer phase change = 6.55033e-10 + D10, D32, Dmax (mu) = 47.0338, 69.538, 181.101 + Liquid penetration 95% mass (m) = 0.0137342 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00595353, Final residual = 2.97048e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.00851692, Final residual = 3.63263e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000545911, Final residual = 4.07257e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000392261, Final residual = 4.05911e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000501743, Final residual = 5.31869e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000501814, Final residual = 5.33352e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000628608, Final residual = 4.2453e-08, No Iterations 1 +min/max(T) = 807.806, 2750 +GAMG: Solving for p, Initial residual = 0.177864, Final residual = 0.000705072, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.88473e-05, global = 1.81609e-05, cumulative = 0.0149879 +GAMG: Solving for p, Initial residual = 0.00071716, Final residual = 6.78464e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.8282e-05, global = 1.82815e-05, cumulative = 0.0150062 +smoothSolver: Solving for epsilon, Initial residual = 0.000752084, Final residual = 1.00074e-07, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000779464, Final residual = 1.66767e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.113091 s +other Time = 1e-06 s +rho Equations = 0.000179 s +U Equations = 0.001185 s +Y Equations = 0.00246113 s +E Equations = 0.000603 s +p Equations = 0.002376 s +calculate parcels = 207.529 s +chemistry correctThermo = 0.002895 s +turbulence correct = 0.001025 s +combustion correct(in Y) = 0.102154 s +percentage of chemistry = 90.3289 % +percentage of rho/U/Y/E = 3.91555 % +========Time details of each equation======= +rhoEqn Time = 0.000338 s +rhoEqn assamble = 0.000266 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001185 s +UEqn assamble = 0.000684 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000501 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001809 s +YEqn assamble = 0.000654 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000172 s +YEqn correct boundary = 0 s +EEqn Time = 0.000445 s +EEqn assamble = 0.000333 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 293.31 s ClockTime = 294 s +Courant Number mean: 0.00605214 max: 0.0215328 +Time = 0.0021725 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21760 + Current mass in system = 1.04952e-09 + Linear momentum = (1.32226e-11 -4.41977e-09 0) + |Linear momentum| = 4.41979e-09 + Linear kinetic energy = 1.04593e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 455.796, 540.2 + Mass transfer phase change = 6.56618e-10 + D10, D32, Dmax (mu) = 46.9876, 69.4929, 180.94 + Liquid penetration 95% mass (m) = 0.0137421 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00524464, Final residual = 9.8668e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00777298, Final residual = 3.44645e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00054243, Final residual = 4.05316e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000391336, Final residual = 4.03307e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000500666, Final residual = 5.28283e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000500729, Final residual = 5.29756e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000624235, Final residual = 4.20443e-08, No Iterations 1 +min/max(T) = 807.772, 2749.92 +GAMG: Solving for p, Initial residual = 0.155761, Final residual = 0.000620037, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.88367e-05, global = 1.81492e-05, cumulative = 0.0150243 +GAMG: Solving for p, Initial residual = 0.000575038, Final residual = 4.92059e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.82723e-05, global = 1.82718e-05, cumulative = 0.0150426 +smoothSolver: Solving for epsilon, Initial residual = 0.000745257, Final residual = 9.88274e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000772526, Final residual = 1.64452e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.115291 s +other Time = 1e-06 s +rho Equations = 0.000236 s +U Equations = 0.001729 s +Y Equations = 0.0022626 s +E Equations = 0.000564 s +p Equations = 0.001723 s +calculate parcels = 207.893 s +chemistry correctThermo = 0.002023 s +turbulence correct = 0.000975 s +combustion correct(in Y) = 0.105532 s +percentage of chemistry = 91.5357 % +percentage of rho/U/Y/E = 4.15609 % +========Time details of each equation======= +rhoEqn Time = 0.00035 s +rhoEqn assamble = 0.000269 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001727 s +UEqn assamble = 0.001031 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000696 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001222 s +YEqn assamble = 0.000518 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -0.00011 s +YEqn correct boundary = 0 s +EEqn Time = 0.000379 s +EEqn assamble = 0.000282 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.7e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 293.79 s ClockTime = 294 s +Courant Number mean: 0.00603338 max: 0.0213006 +Time = 0.002175 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21757 + Current mass in system = 1.04794e-09 + Linear momentum = (1.30457e-11 -4.41193e-09 0) + |Linear momentum| = 4.41195e-09 + Linear kinetic energy = 1.04358e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 455.961, 540.2 + Mass transfer phase change = 6.58206e-10 + D10, D32, Dmax (mu) = 46.9798, 69.4491, 180.924 + Liquid penetration 95% mass (m) = 0.0137504 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00437701, Final residual = 8.05888e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00702469, Final residual = 3.24611e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000539468, Final residual = 4.04309e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000389762, Final residual = 3.99217e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000498622, Final residual = 5.22774e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000498678, Final residual = 5.24212e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000620075, Final residual = 4.16556e-08, No Iterations 1 +min/max(T) = 807.741, 2749.85 +GAMG: Solving for p, Initial residual = 0.125272, Final residual = 0.000493532, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.88405e-05, global = 1.81738e-05, cumulative = 0.0150608 +GAMG: Solving for p, Initial residual = 0.00045733, Final residual = 3.30015e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.82959e-05, global = 1.82955e-05, cumulative = 0.0150791 +smoothSolver: Solving for epsilon, Initial residual = 0.000738337, Final residual = 9.75725e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000765042, Final residual = 1.61817e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.101152 s +other Time = 1e-06 s +rho Equations = 0.000175 s +U Equations = 0.00115 s +Y Equations = 0.0024975 s +E Equations = 0.000582 s +p Equations = 0.0023 s +calculate parcels = 208.255 s +chemistry correctThermo = 0.002876 s +turbulence correct = 0.000995 s +combustion correct(in Y) = 0.0903785 s +percentage of chemistry = 89.3492 % +percentage of rho/U/Y/E = 4.35434 % +========Time details of each equation======= +rhoEqn Time = 0.000317 s +rhoEqn assamble = 0.000248 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00115 s +UEqn assamble = 0.000708 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000442 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001874 s +YEqn assamble = 0.00066 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000201 s +YEqn correct boundary = 0 s +EEqn Time = 0.000431 s +EEqn assamble = 0.000321 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.00011 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 294.25 s ClockTime = 295 s +Courant Number mean: 0.00600534 max: 0.0210009 +Time = 0.0021775 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21757 + Current mass in system = 1.04635e-09 + Linear momentum = (1.28867e-11 -4.40401e-09 0) + |Linear momentum| = 4.40403e-09 + Linear kinetic energy = 1.0412e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 456.127, 540.2 + Mass transfer phase change = 6.59789e-10 + D10, D32, Dmax (mu) = 46.9177, 69.4031, 181.206 + Liquid penetration 95% mass (m) = 0.0137575 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00400416, Final residual = 7.82674e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00680399, Final residual = 3.18985e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000535536, Final residual = 4.00863e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000387946, Final residual = 3.94055e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00049694, Final residual = 5.16563e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000496989, Final residual = 5.17988e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000616196, Final residual = 4.12428e-08, No Iterations 1 +min/max(T) = 807.713, 2749.78 +GAMG: Solving for p, Initial residual = 0.102882, Final residual = 0.000400609, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.87931e-05, global = 1.81299e-05, cumulative = 0.0150972 +GAMG: Solving for p, Initial residual = 0.000376163, Final residual = 2.98695e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.8254e-05, global = 1.82536e-05, cumulative = 0.0151155 +smoothSolver: Solving for epsilon, Initial residual = 0.000730962, Final residual = 9.62863e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000757167, Final residual = 1.59008e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102135 s +other Time = 0 s +rho Equations = 0.000182 s +U Equations = 0.001163 s +Y Equations = 0.00249465 s +E Equations = 0.000611 s +p Equations = 0.002822 s +calculate parcels = 208.602 s +chemistry correctThermo = 0.002915 s +turbulence correct = 0.001249 s +combustion correct(in Y) = 0.0904804 s +percentage of chemistry = 88.589 % +percentage of rho/U/Y/E = 4.35761 % +========Time details of each equation======= +rhoEqn Time = 0.000359 s +rhoEqn assamble = 0.000284 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001162 s +UEqn assamble = 0.000713 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000449 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001835 s +YEqn assamble = 0.000656 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000189 s +YEqn correct boundary = 0 s +EEqn Time = 0.000451 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 294.7 s ClockTime = 295 s +Courant Number mean: 0.00596815 max: 0.0206982 +Time = 0.00218 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21756 + Current mass in system = 1.04477e-09 + Linear momentum = (1.2745e-11 -4.39602e-09 0) + |Linear momentum| = 4.39604e-09 + Linear kinetic energy = 1.03879e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 456.293, 540.2 + Mass transfer phase change = 6.61375e-10 + D10, D32, Dmax (mu) = 46.8757, 69.3576, 181.486 + Liquid penetration 95% mass (m) = 0.0137661 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00432904, Final residual = 9.24832e-07, No Iterations 1 +smoothSolver: Solving for Uy, Initial residual = 0.00871628, Final residual = 3.96273e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000532771, Final residual = 3.99274e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000385623, Final residual = 3.87898e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000494093, Final residual = 5.08951e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000494135, Final residual = 5.10365e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000613057, Final residual = 4.08522e-08, No Iterations 1 +min/max(T) = 807.686, 2749.7 +GAMG: Solving for p, Initial residual = 0.0869188, Final residual = 0.000325408, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.87913e-05, global = 1.8157e-05, cumulative = 0.0151336 +GAMG: Solving for p, Initial residual = 0.000310495, Final residual = 2.0004e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.82736e-05, global = 1.82732e-05, cumulative = 0.0151519 +smoothSolver: Solving for epsilon, Initial residual = 0.000723789, Final residual = 9.49403e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000748836, Final residual = 1.56008e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.078091 s +other Time = 1e-06 s +rho Equations = 0.000172 s +U Equations = 0.000975 s +Y Equations = 0.00216878 s +E Equations = 0.000481 s +p Equations = 0.001967 s +calculate parcels = 208.864 s +chemistry correctThermo = 0.002082 s +turbulence correct = 0.000842 s +combustion correct(in Y) = 0.0692092 s +percentage of chemistry = 88.6264 % +percentage of rho/U/Y/E = 4.862 % +========Time details of each equation======= +rhoEqn Time = 0.000315 s +rhoEqn assamble = 0.00024 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.000974 s +UEqn assamble = 0.000616 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000358 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001535 s +YEqn assamble = 0.000541 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000105 s +YEqn correct boundary = 0 s +EEqn Time = 0.000361 s +EEqn assamble = 0.000272 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 8.9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 295.04 s ClockTime = 296 s +Courant Number mean: 0.00592199 max: 0.0203266 +Time = 0.0021825 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21755 + Current mass in system = 1.04318e-09 + Linear momentum = (1.26209e-11 -4.38796e-09 0) + |Linear momentum| = 4.38798e-09 + Linear kinetic energy = 1.03636e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 456.459, 540.2 + Mass transfer phase change = 6.62962e-10 + D10, D32, Dmax (mu) = 46.8414, 69.3122, 181.763 + Liquid penetration 95% mass (m) = 0.0137727 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00498535, Final residual = 3.10996e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0107292, Final residual = 4.7681e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000530581, Final residual = 3.96678e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00038291, Final residual = 3.80768e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000490746, Final residual = 5.00129e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000490795, Final residual = 5.01525e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000609978, Final residual = 4.04568e-08, No Iterations 1 +min/max(T) = 807.661, 2749.62 +GAMG: Solving for p, Initial residual = 0.0749899, Final residual = 0.000274639, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.878e-05, global = 1.81792e-05, cumulative = 0.0151701 +GAMG: Solving for p, Initial residual = 0.000264043, Final residual = 2.45414e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.82904e-05, global = 1.82899e-05, cumulative = 0.0151884 +smoothSolver: Solving for epsilon, Initial residual = 0.000717404, Final residual = 9.358e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000740516, Final residual = 1.52935e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100072 s +other Time = 0 s +rho Equations = 0.000186 s +U Equations = 0.001183 s +Y Equations = 0.0024511 s +E Equations = 0.0006 s +p Equations = 0.0023 s +calculate parcels = 209.202 s +chemistry correctThermo = 0.002843 s +turbulence correct = 0.000989 s +combustion correct(in Y) = 0.0893189 s +percentage of chemistry = 89.2546 % +percentage of rho/U/Y/E = 4.41692 % +========Time details of each equation======= +rhoEqn Time = 0.000334 s +rhoEqn assamble = 0.000264 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001182 s +UEqn assamble = 0.000688 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000494 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001757 s +YEqn assamble = 0.000633 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000146 s +YEqn correct boundary = 0 s +EEqn Time = 0.000445 s +EEqn assamble = 0.000332 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 295.48 s ClockTime = 296 s +Courant Number mean: 0.00586709 max: 0.0199671 +Time = 0.002185 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21753 + Current mass in system = 1.04159e-09 + Linear momentum = (1.25196e-11 -4.37983e-09 0) + |Linear momentum| = 4.37985e-09 + Linear kinetic energy = 1.0339e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 456.626, 540.2 + Mass transfer phase change = 6.64551e-10 + D10, D32, Dmax (mu) = 46.7996, 69.2669, 182.035 + Liquid penetration 95% mass (m) = 0.0137802 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00591551, Final residual = 3.68573e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.012714, Final residual = 5.55149e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000528319, Final residual = 3.93187e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000380014, Final residual = 3.7274e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000487287, Final residual = 4.90087e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000487331, Final residual = 4.91459e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000607026, Final residual = 4.00515e-08, No Iterations 1 +min/max(T) = 807.637, 2749.53 +GAMG: Solving for p, Initial residual = 0.0657062, Final residual = 0.000242731, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.87995e-05, global = 1.82017e-05, cumulative = 0.0152066 +GAMG: Solving for p, Initial residual = 0.000234439, Final residual = 2.44761e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.83144e-05, global = 1.83139e-05, cumulative = 0.0152249 +smoothSolver: Solving for epsilon, Initial residual = 0.00071182, Final residual = 9.21988e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000732064, Final residual = 1.49761e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103016 s +other Time = 0 s +rho Equations = 0.000179 s +U Equations = 0.001232 s +Y Equations = 0.00249925 s +E Equations = 0.000601 s +p Equations = 0.002425 s +calculate parcels = 209.571 s +chemistry correctThermo = 0.002893 s +turbulence correct = 0.001077 s +combustion correct(in Y) = 0.0919008 s +percentage of chemistry = 89.2102 % +percentage of rho/U/Y/E = 4.37917 % +========Time details of each equation======= +rhoEqn Time = 0.000332 s +rhoEqn assamble = 0.000262 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001231 s +UEqn assamble = 0.000724 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000507 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001869 s +YEqn assamble = 0.000652 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000208 s +YEqn correct boundary = 0 s +EEqn Time = 0.000445 s +EEqn assamble = 0.00033 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 295.95 s ClockTime = 297 s +Courant Number mean: 0.0058039 max: 0.0195114 +Time = 0.0021875 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21752 + Current mass in system = 1.04e-09 + Linear momentum = (1.2445e-11 -4.37164e-09 0) + |Linear momentum| = 4.37166e-09 + Linear kinetic energy = 1.03142e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 456.793, 540.2 + Mass transfer phase change = 6.6614e-10 + D10, D32, Dmax (mu) = 46.7631, 69.2208, 182.302 + Liquid penetration 95% mass (m) = 0.0137878 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00669219, Final residual = 4.21069e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.014682, Final residual = 6.31607e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000527119, Final residual = 3.91236e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000376554, Final residual = 3.63763e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0004836, Final residual = 4.79653e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000483637, Final residual = 4.81029e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000604078, Final residual = 3.9641e-08, No Iterations 1 +min/max(T) = 807.613, 2749.41 +GAMG: Solving for p, Initial residual = 0.0582263, Final residual = 0.000206654, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.87919e-05, global = 1.8213e-05, cumulative = 0.0152431 +GAMG: Solving for p, Initial residual = 0.000200222, Final residual = 2.00991e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.83171e-05, global = 1.83166e-05, cumulative = 0.0152614 +smoothSolver: Solving for epsilon, Initial residual = 0.000706361, Final residual = 9.07871e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000723692, Final residual = 1.46515e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.079625 s +other Time = 1e-06 s +rho Equations = 0.000156 s +U Equations = 0.001148 s +Y Equations = 0.00216908 s +E Equations = 0.000511 s +p Equations = 0.001792 s +calculate parcels = 209.887 s +chemistry correctThermo = 0.00204 s +turbulence correct = 0.000856 s +combustion correct(in Y) = 0.0707729 s +percentage of chemistry = 88.8828 % +percentage of rho/U/Y/E = 5.00355 % +========Time details of each equation======= +rhoEqn Time = 0.000272 s +rhoEqn assamble = 0.000215 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001147 s +UEqn assamble = 0.000685 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000462 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001604 s +YEqn assamble = 0.000543 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000159 s +YEqn correct boundary = 0 s +EEqn Time = 0.000389 s +EEqn assamble = 0.000277 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 296.35 s ClockTime = 297 s +Courant Number mean: 0.00573228 max: 0.0190765 +Time = 0.00219 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21750 + Current mass in system = 1.03841e-09 + Linear momentum = (1.23992e-11 -4.3634e-09 0) + |Linear momentum| = 4.36342e-09 + Linear kinetic energy = 1.02892e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 456.961, 540.2 + Mass transfer phase change = 6.67733e-10 + D10, D32, Dmax (mu) = 46.7342, 69.1755, 182.564 + Liquid penetration 95% mass (m) = 0.013795 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00715337, Final residual = 4.50814e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.016625, Final residual = 7.05455e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00052403, Final residual = 3.88524e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.0003727, Final residual = 3.53842e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000478608, Final residual = 4.67389e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000478635, Final residual = 4.68732e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000599834, Final residual = 3.9054e-08, No Iterations 1 +min/max(T) = 807.587, 2749.28 +GAMG: Solving for p, Initial residual = 0.0520476, Final residual = 0.000185468, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.88423e-05, global = 1.82685e-05, cumulative = 0.0152797 +GAMG: Solving for p, Initial residual = 0.000179582, Final residual = 1.64785e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.83655e-05, global = 1.8365e-05, cumulative = 0.015298 +smoothSolver: Solving for epsilon, Initial residual = 0.000700655, Final residual = 8.94444e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000714932, Final residual = 1.43221e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.094156 s +other Time = 0 s +rho Equations = 0.000181 s +U Equations = 0.001154 s +Y Equations = 0.00253332 s +E Equations = 0.000615 s +p Equations = 0.002289 s +calculate parcels = 210.2 s +chemistry correctThermo = 0.002879 s +turbulence correct = 0.001102 s +combustion correct(in Y) = 0.0832007 s +percentage of chemistry = 88.3647 % +percentage of rho/U/Y/E = 4.76159 % +========Time details of each equation======= +rhoEqn Time = 0.000328 s +rhoEqn assamble = 0.000257 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001153 s +UEqn assamble = 0.000659 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000494 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001893 s +YEqn assamble = 0.000659 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000189 s +YEqn correct boundary = 0 s +EEqn Time = 0.000455 s +EEqn assamble = 0.000328 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000127 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 296.76 s ClockTime = 297 s +Courant Number mean: 0.0056528 max: 0.0186658 +Time = 0.0021925 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21749 + Current mass in system = 1.03682e-09 + Linear momentum = (1.23858e-11 -4.35511e-09 0) + |Linear momentum| = 4.35513e-09 + Linear kinetic energy = 1.0264e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 457.129, 540.2 + Mass transfer phase change = 6.69327e-10 + D10, D32, Dmax (mu) = 46.6883, 69.129, 182.819 + Liquid penetration 95% mass (m) = 0.0138019 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00767892, Final residual = 4.75164e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0185448, Final residual = 7.75893e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000522427, Final residual = 3.85523e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000368707, Final residual = 3.43756e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000474012, Final residual = 4.55662e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00047404, Final residual = 4.5697e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000595701, Final residual = 3.8499e-08, No Iterations 1 +min/max(T) = 807.563, 2749.14 +GAMG: Solving for p, Initial residual = 0.0468645, Final residual = 0.000163121, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.88369e-05, global = 1.82739e-05, cumulative = 0.0153163 +GAMG: Solving for p, Initial residual = 0.00015909, Final residual = 9.46623e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.83683e-05, global = 1.83653e-05, cumulative = 0.0153347 +smoothSolver: Solving for epsilon, Initial residual = 0.000694957, Final residual = 8.81015e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000706632, Final residual = 1.40002e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.101681 s +other Time = 1e-06 s +rho Equations = 0.000188 s +U Equations = 0.001185 s +Y Equations = 0.00229135 s +E Equations = 0.000533 s +p Equations = 0.001785 s +calculate parcels = 210.537 s +chemistry correctThermo = 0.002033 s +turbulence correct = 0.000951 s +combustion correct(in Y) = 0.0924977 s +percentage of chemistry = 90.9685 % +percentage of rho/U/Y/E = 4.12796 % +========Time details of each equation======= +rhoEqn Time = 0.000315 s +rhoEqn assamble = 0.000249 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001185 s +UEqn assamble = 0.000682 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000503 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001637 s +YEqn assamble = 0.000572 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000141 s +YEqn correct boundary = 0 s +EEqn Time = 0.000408 s +EEqn assamble = 0.000312 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 297.19 s ClockTime = 298 s +Courant Number mean: 0.00556573 max: 0.0183271 +Time = 0.002195 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21746 + Current mass in system = 1.03522e-09 + Linear momentum = (1.24053e-11 -4.34677e-09 0) + |Linear momentum| = 4.34679e-09 + Linear kinetic energy = 1.02387e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 457.297, 540.2 + Mass transfer phase change = 6.70924e-10 + D10, D32, Dmax (mu) = 46.6771, 69.0831, 182.957 + Liquid penetration 95% mass (m) = 0.0138098 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00781159, Final residual = 4.81986e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0204499, Final residual = 8.43442e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000520136, Final residual = 3.8109e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000364565, Final residual = 3.33357e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000468636, Final residual = 4.43064e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000468658, Final residual = 4.44335e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000591025, Final residual = 3.78554e-08, No Iterations 1 +min/max(T) = 807.54, 2748.98 +GAMG: Solving for p, Initial residual = 0.0423726, Final residual = 0.000139327, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.88587e-05, global = 1.83263e-05, cumulative = 0.015353 +GAMG: Solving for p, Initial residual = 0.000136206, Final residual = 8.02454e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.84143e-05, global = 1.84115e-05, cumulative = 0.0153714 +smoothSolver: Solving for epsilon, Initial residual = 0.000689118, Final residual = 8.67626e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000698463, Final residual = 1.36855e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.098296 s +other Time = 0 s +rho Equations = 0.000182 s +U Equations = 0.001073 s +Y Equations = 0.00272073 s +E Equations = 0.000652 s +p Equations = 0.00266 s +calculate parcels = 210.8 s +chemistry correctThermo = 0.002957 s +turbulence correct = 0.001105 s +combustion correct(in Y) = 0.0867033 s +percentage of chemistry = 88.2063 % +percentage of rho/U/Y/E = 4.70795 % +========Time details of each equation======= +rhoEqn Time = 0.000346 s +rhoEqn assamble = 0.000275 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001071 s +UEqn assamble = 0.000642 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000429 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002135 s +YEqn assamble = 0.000743 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000237 s +YEqn correct boundary = 0 s +EEqn Time = 0.000471 s +EEqn assamble = 0.000355 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000116 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 297.56 s ClockTime = 298 s +Courant Number mean: 0.00547142 max: 0.0179718 +Time = 0.0021975 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21744 + Current mass in system = 1.03362e-09 + Linear momentum = (1.2457e-11 -4.33839e-09 0) + |Linear momentum| = 4.33841e-09 + Linear kinetic energy = 1.02133e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 457.465, 540.2 + Mass transfer phase change = 6.72524e-10 + D10, D32, Dmax (mu) = 46.6505, 69.0367, 182.8 + Liquid penetration 95% mass (m) = 0.0138178 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00788201, Final residual = 4.81243e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0223325, Final residual = 9.07584e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000518007, Final residual = 3.76366e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000360494, Final residual = 3.22831e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000463426, Final residual = 4.3043e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000463442, Final residual = 4.31664e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000586345, Final residual = 3.71988e-08, No Iterations 1 +min/max(T) = 807.518, 2748.81 +GAMG: Solving for p, Initial residual = 0.038542, Final residual = 0.000123177, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.88643e-05, global = 1.83608e-05, cumulative = 0.0153898 +GAMG: Solving for p, Initial residual = 0.000120766, Final residual = 7.78038e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.84434e-05, global = 1.84406e-05, cumulative = 0.0154082 +smoothSolver: Solving for epsilon, Initial residual = 0.000683294, Final residual = 8.54394e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000690726, Final residual = 1.33855e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100158 s +other Time = 0 s +rho Equations = 0.000208 s +U Equations = 0.00128 s +Y Equations = 0.00223711 s +E Equations = 0.000498 s +p Equations = 0.001662 s +calculate parcels = 211.148 s +chemistry correctThermo = 0.002047 s +turbulence correct = 0.000839 s +combustion correct(in Y) = 0.0911779 s +percentage of chemistry = 91.0341 % +percentage of rho/U/Y/E = 4.21645 % +========Time details of each equation======= +rhoEqn Time = 0.000328 s +rhoEqn assamble = 0.000257 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001279 s +UEqn assamble = 0.000758 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000521 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001568 s +YEqn assamble = 0.000567 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000104 s +YEqn correct boundary = 0 s +EEqn Time = 0.000374 s +EEqn assamble = 0.000278 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 298 s ClockTime = 299 s +Courant Number mean: 0.00537027 max: 0.0176182 +Time = 0.0022 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21740 + Current mass in system = 1.03197e-09 + Linear momentum = (1.25792e-11 -4.32994e-09 0) + |Linear momentum| = 4.32996e-09 + Linear kinetic energy = 1.01877e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 457.634, 540.2 + Mass transfer phase change = 6.74177e-10 + D10, D32, Dmax (mu) = 46.6408, 68.9949, 183.212 + Liquid penetration 95% mass (m) = 0.0138261 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00791789, Final residual = 4.74296e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0241997, Final residual = 9.6854e-10, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000529894, Final residual = 3.9291e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000356396, Final residual = 3.12213e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000459863, Final residual = 4.21715e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000459874, Final residual = 4.22945e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000582482, Final residual = 3.68112e-08, No Iterations 1 +min/max(T) = 807.497, 2748.63 +GAMG: Solving for p, Initial residual = 0.0354626, Final residual = 0.00024315, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.96075e-05, global = 1.8882e-05, cumulative = 0.0154271 +GAMG: Solving for p, Initial residual = 0.000229797, Final residual = 2.26407e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.90493e-05, global = 1.90488e-05, cumulative = 0.0154461 +smoothSolver: Solving for epsilon, Initial residual = 0.000684255, Final residual = 8.50085e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00068818, Final residual = 1.32074e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.116508 s +other Time = 0 s +rho Equations = 0.000179 s +U Equations = 0.001192 s +Y Equations = 0.00274184 s +E Equations = 0.000662 s +p Equations = 0.002804 s +calculate parcels = 211.52 s +chemistry correctThermo = 0.003149 s +turbulence correct = 0.001215 s +combustion correct(in Y) = 0.104376 s +percentage of chemistry = 89.5871 % +percentage of rho/U/Y/E = 4.09829 % +========Time details of each equation======= +rhoEqn Time = 0.000335 s +rhoEqn assamble = 0.000261 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001191 s +UEqn assamble = 0.000661 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00053 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002069 s +YEqn assamble = 0.000765 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000233 s +YEqn correct boundary = 0 s +EEqn Time = 0.000506 s +EEqn assamble = 0.000385 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000121 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 298.82 s ClockTime = 299 s +Courant Number mean: 0.00526539 max: 0.0172298 +Time = 0.0022025 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21738 + Current mass in system = 1.03036e-09 + Linear momentum = (1.27346e-11 -4.32144e-09 0) + |Linear momentum| = 4.32146e-09 + Linear kinetic energy = 1.01619e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 457.802, 540.2 + Mass transfer phase change = 6.75783e-10 + D10, D32, Dmax (mu) = 46.6211, 68.9475, 183.649 + Liquid penetration 95% mass (m) = 0.0138332 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0118045, Final residual = 6.92017e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0263093, Final residual = 1.03842e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000518615, Final residual = 3.68168e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000350022, Final residual = 3.01572e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000450304, Final residual = 4.05115e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000450318, Final residual = 4.06245e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000578551, Final residual = 3.5878e-08, No Iterations 1 +min/max(T) = 807.477, 2748.41 +GAMG: Solving for p, Initial residual = 0.033336, Final residual = 0.000284744, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.93807e-05, global = 1.84821e-05, cumulative = 0.0154646 +GAMG: Solving for p, Initial residual = 0.00026969, Final residual = 2.51545e-07, No Iterations 4 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.85187e-05, global = 1.85178e-05, cumulative = 0.0154831 +smoothSolver: Solving for epsilon, Initial residual = 0.000671225, Final residual = 8.27758e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000678904, Final residual = 1.28404e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.107846 s +other Time = 0 s +rho Equations = 0.000195 s +U Equations = 0.001225 s +Y Equations = 0.00252984 s +E Equations = 0.000607 s +p Equations = 0.002406 s +calculate parcels = 211.852 s +chemistry correctThermo = 0.002867 s +turbulence correct = 0.000963 s +combustion correct(in Y) = 0.0967882 s +percentage of chemistry = 89.7466 % +percentage of rho/U/Y/E = 4.22532 % +========Time details of each equation======= +rhoEqn Time = 0.00034 s +rhoEqn assamble = 0.00027 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001223 s +UEqn assamble = 0.000705 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000518 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001771 s +YEqn assamble = 0.000658 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00015 s +YEqn correct boundary = 0 s +EEqn Time = 0.00045 s +EEqn assamble = 0.000336 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 299.26 s ClockTime = 300 s +Courant Number mean: 0.00515156 max: 0.0170225 +Time = 0.002205 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21735 + Current mass in system = 1.02875e-09 + Linear momentum = (1.2928e-11 -4.31289e-09 0) + |Linear momentum| = 4.31291e-09 + Linear kinetic energy = 1.0136e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 457.969, 540.2 + Mass transfer phase change = 6.77397e-10 + D10, D32, Dmax (mu) = 46.6294, 68.9005, 184.074 + Liquid penetration 95% mass (m) = 0.0138401 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0115431, Final residual = 6.52645e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0280891, Final residual = 1.09049e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000518317, Final residual = 3.63164e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000345305, Final residual = 2.89362e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000444564, Final residual = 3.91268e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000444573, Final residual = 3.92361e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000573048, Final residual = 3.50794e-08, No Iterations 1 +min/max(T) = 807.457, 2748.13 +GAMG: Solving for p, Initial residual = 0.0302979, Final residual = 0.000185596, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.92366e-05, global = 1.85413e-05, cumulative = 0.0155017 +GAMG: Solving for p, Initial residual = 0.000174976, Final residual = 6.4126e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.86032e-05, global = 1.86008e-05, cumulative = 0.0155203 +smoothSolver: Solving for epsilon, Initial residual = 0.000668408, Final residual = 8.17205e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000675494, Final residual = 1.25903e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.080668 s +other Time = 0 s +rho Equations = 0.000173 s +U Equations = 0.001156 s +Y Equations = 0.00215752 s +E Equations = 0.000489 s +p Equations = 0.001876 s +calculate parcels = 212.215 s +chemistry correctThermo = 0.002002 s +turbulence correct = 0.000921 s +combustion correct(in Y) = 0.0716975 s +percentage of chemistry = 88.8797 % +percentage of rho/U/Y/E = 4.92825 % +========Time details of each equation======= +rhoEqn Time = 0.000307 s +rhoEqn assamble = 0.000246 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001154 s +UEqn assamble = 0.000741 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000413 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001588 s +YEqn assamble = 0.000538 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000137 s +YEqn correct boundary = 0 s +EEqn Time = 0.000364 s +EEqn assamble = 0.000273 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 299.7 s ClockTime = 300 s +Courant Number mean: 0.0050301 max: 0.0169555 +Time = 0.0022075 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21733 + Current mass in system = 1.02713e-09 + Linear momentum = (1.31331e-11 -4.30432e-09 0) + |Linear momentum| = 4.30434e-09 + Linear kinetic energy = 1.011e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 458.137, 540.2 + Mass transfer phase change = 6.79011e-10 + D10, D32, Dmax (mu) = 46.6056, 68.8519, 184.336 + Liquid penetration 95% mass (m) = 0.0138473 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0108238, Final residual = 6.13739e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0298784, Final residual = 1.14253e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000515711, Final residual = 3.58384e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000340608, Final residual = 2.76789e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000439045, Final residual = 3.76978e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000439039, Final residual = 3.78034e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000565115, Final residual = 3.42015e-08, No Iterations 1 +min/max(T) = 807.438, 2747.84 +GAMG: Solving for p, Initial residual = 0.0275748, Final residual = 0.00014491, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.91883e-05, global = 1.85303e-05, cumulative = 0.0155388 +GAMG: Solving for p, Initial residual = 0.000134349, Final residual = 3.71087e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.86006e-05, global = 1.85993e-05, cumulative = 0.0155574 +smoothSolver: Solving for epsilon, Initial residual = 0.000664999, Final residual = 8.07781e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000670557, Final residual = 1.23288e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.107553 s +other Time = 0 s +rho Equations = 0.000191 s +U Equations = 0.001216 s +Y Equations = 0.00243122 s +E Equations = 0.000601 s +p Equations = 0.002296 s +calculate parcels = 212.49 s +chemistry correctThermo = 0.0029 s +turbulence correct = 0.00103 s +combustion correct(in Y) = 0.0966508 s +percentage of chemistry = 89.8634 % +percentage of rho/U/Y/E = 4.12747 % +========Time details of each equation======= +rhoEqn Time = 0.000335 s +rhoEqn assamble = 0.000264 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001215 s +UEqn assamble = 0.000767 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000448 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001822 s +YEqn assamble = 0.000639 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000199 s +YEqn correct boundary = 0 s +EEqn Time = 0.000448 s +EEqn assamble = 0.000326 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000122 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 300.09 s ClockTime = 301 s +Courant Number mean: 0.0049025 max: 0.016877 +Time = 0.00221 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21729 + Current mass in system = 1.02552e-09 + Linear momentum = (1.33402e-11 -4.29574e-09 0) + |Linear momentum| = 4.29576e-09 + Linear kinetic energy = 1.0084e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 458.305, 540.2 + Mass transfer phase change = 6.80626e-10 + D10, D32, Dmax (mu) = 46.6197, 68.8044, 184.206 + Liquid penetration 95% mass (m) = 0.0138548 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0103372, Final residual = 5.90825e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0316701, Final residual = 1.1902e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000513419, Final residual = 3.54647e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000336055, Final residual = 2.65648e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000433383, Final residual = 3.64342e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000433378, Final residual = 3.65363e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000558259, Final residual = 3.35379e-08, No Iterations 1 +min/max(T) = 807.418, 2747.6 +GAMG: Solving for p, Initial residual = 0.025471, Final residual = 0.000118349, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.91428e-05, global = 1.85559e-05, cumulative = 0.015576 +GAMG: Solving for p, Initial residual = 0.000111169, Final residual = 3.06935e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.86166e-05, global = 1.86156e-05, cumulative = 0.0155946 +smoothSolver: Solving for epsilon, Initial residual = 0.000662653, Final residual = 7.98899e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.00066618, Final residual = 1.20829e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.112237 s +other Time = 0 s +rho Equations = 0.000164 s +U Equations = 0.001103 s +Y Equations = 0.00243333 s +E Equations = 0.000604 s +p Equations = 0.002275 s +calculate parcels = 212.842 s +chemistry correctThermo = 0.002909 s +turbulence correct = 0.000969 s +combustion correct(in Y) = 0.101586 s +percentage of chemistry = 90.51 % +percentage of rho/U/Y/E = 3.83504 % +========Time details of each equation======= +rhoEqn Time = 0.000312 s +rhoEqn assamble = 0.000244 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001103 s +UEqn assamble = 0.000685 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000418 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001884 s +YEqn assamble = 0.000643 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000247 s +YEqn correct boundary = 0 s +EEqn Time = 0.000446 s +EEqn assamble = 0.000334 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 300.55 s ClockTime = 301 s +Courant Number mean: 0.00477035 max: 0.016762 +Time = 0.0022125 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21729 + Current mass in system = 1.02391e-09 + Linear momentum = (1.35464e-11 -4.28719e-09 0) + |Linear momentum| = 4.28721e-09 + Linear kinetic energy = 1.00581e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 458.474, 540.2 + Mass transfer phase change = 6.82237e-10 + D10, D32, Dmax (mu) = 46.5545, 68.7544, 184.075 + Liquid penetration 95% mass (m) = 0.013862 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00998952, Final residual = 5.6889e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0334476, Final residual = 1.23239e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000511553, Final residual = 3.52322e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000331016, Final residual = 2.55252e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000427732, Final residual = 3.5237e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000427717, Final residual = 3.53358e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000552053, Final residual = 3.29618e-08, No Iterations 1 +min/max(T) = 807.398, 2747.42 +GAMG: Solving for p, Initial residual = 0.023676, Final residual = 0.000106817, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.90504e-05, global = 1.85087e-05, cumulative = 0.0156131 +GAMG: Solving for p, Initial residual = 0.000101086, Final residual = 2.09399e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.85647e-05, global = 1.85638e-05, cumulative = 0.0156317 +smoothSolver: Solving for epsilon, Initial residual = 0.00066074, Final residual = 7.90483e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000662542, Final residual = 1.18591e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092296 s +other Time = 1e-06 s +rho Equations = 0.000148 s +U Equations = 0.001278 s +Y Equations = 0.00256125 s +E Equations = 0.000623 s +p Equations = 0.002356 s +calculate parcels = 213.182 s +chemistry correctThermo = 0.002917 s +turbulence correct = 0.001112 s +combustion correct(in Y) = 0.0811287 s +percentage of chemistry = 87.9006 % +percentage of rho/U/Y/E = 4.99507 % +========Time details of each equation======= +rhoEqn Time = 0.000305 s +rhoEqn assamble = 0.00024 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001276 s +UEqn assamble = 0.00076 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000516 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001915 s +YEqn assamble = 0.000699 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000216 s +YEqn correct boundary = 0 s +EEqn Time = 0.000463 s +EEqn assamble = 0.000344 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000119 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 300.98 s ClockTime = 302 s +Courant Number mean: 0.00463431 max: 0.0166332 +Time = 0.002215 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21726 + Current mass in system = 1.02229e-09 + Linear momentum = (1.37535e-11 -4.27864e-09 0) + |Linear momentum| = 4.27866e-09 + Linear kinetic energy = 1.00321e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 458.643, 540.2 + Mass transfer phase change = 6.83852e-10 + D10, D32, Dmax (mu) = 46.5434, 68.7064, 183.943 + Liquid penetration 95% mass (m) = 0.0138713 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00960926, Final residual = 5.3872e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0352213, Final residual = 1.27094e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000512145, Final residual = 3.50726e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000326197, Final residual = 2.45505e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000421759, Final residual = 3.40783e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000421752, Final residual = 3.4173e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000546676, Final residual = 3.23862e-08, No Iterations 1 +min/max(T) = 807.378, 2747.25 +GAMG: Solving for p, Initial residual = 0.0220702, Final residual = 9.31728e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.90644e-05, global = 1.85687e-05, cumulative = 0.0156502 +GAMG: Solving for p, Initial residual = 8.94117e-05, Final residual = 9.41883e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.86238e-05, global = 1.8619e-05, cumulative = 0.0156689 +smoothSolver: Solving for epsilon, Initial residual = 0.000659417, Final residual = 7.82882e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000659583, Final residual = 1.16589e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097202 s +other Time = 0 s +rho Equations = 0.000187 s +U Equations = 0.00121 s +Y Equations = 0.00258343 s +E Equations = 0.000602 s +p Equations = 0.002367 s +calculate parcels = 213.533 s +chemistry correctThermo = 0.00293 s +turbulence correct = 0.001156 s +combustion correct(in Y) = 0.0859506 s +percentage of chemistry = 88.4247 % +percentage of rho/U/Y/E = 4.71434 % +========Time details of each equation======= +rhoEqn Time = 0.000347 s +rhoEqn assamble = 0.000275 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001209 s +UEqn assamble = 0.000685 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000524 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001939 s +YEqn assamble = 0.000685 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000199 s +YEqn correct boundary = 0 s +EEqn Time = 0.000442 s +EEqn assamble = 0.000328 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000114 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 301.43 s ClockTime = 302 s +Courant Number mean: 0.00449437 max: 0.016523 +Time = 0.0022175 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21723 + Current mass in system = 1.02067e-09 + Linear momentum = (1.39621e-11 -4.27009e-09 0) + |Linear momentum| = 4.27011e-09 + Linear kinetic energy = 1.00062e-08 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 458.813, 540.2 + Mass transfer phase change = 6.85469e-10 + D10, D32, Dmax (mu) = 46.5261, 68.6581, 183.812 + Liquid penetration 95% mass (m) = 0.0138786 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00966016, Final residual = 5.34798e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0369776, Final residual = 1.3068e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000511904, Final residual = 3.49948e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000321139, Final residual = 2.36054e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000416025, Final residual = 3.29877e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000416013, Final residual = 3.30799e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000541333, Final residual = 3.18205e-08, No Iterations 1 +min/max(T) = 807.358, 2747.08 +GAMG: Solving for p, Initial residual = 0.0206685, Final residual = 8.9347e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.90891e-05, global = 1.85849e-05, cumulative = 0.0156874 +GAMG: Solving for p, Initial residual = 8.60185e-05, Final residual = 9.11724e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.86418e-05, global = 1.86367e-05, cumulative = 0.0157061 +smoothSolver: Solving for epsilon, Initial residual = 0.000657181, Final residual = 7.74222e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000656668, Final residual = 1.14615e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.101898 s +other Time = 0 s +rho Equations = 0.000189 s +U Equations = 0.001312 s +Y Equations = 0.00225905 s +E Equations = 0.000598 s +p Equations = 0.001982 s +calculate parcels = 213.846 s +chemistry correctThermo = 0.002909 s +turbulence correct = 0.000806 s +combustion correct(in Y) = 0.091635 s +percentage of chemistry = 89.9281 % +percentage of rho/U/Y/E = 4.27687 % +========Time details of each equation======= +rhoEqn Time = 0.000326 s +rhoEqn assamble = 0.000257 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001312 s +UEqn assamble = 0.00079 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000522 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001561 s +YEqn assamble = 0.000567 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000112 s +YEqn correct boundary = 0 s +EEqn Time = 0.000441 s +EEqn assamble = 0.000328 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 301.85 s ClockTime = 302 s +Courant Number mean: 0.00435013 max: 0.0163969 +Time = 0.00222 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21721 + Current mass in system = 1.01906e-09 + Linear momentum = (1.41729e-11 -4.26153e-09 0) + |Linear momentum| = 4.26156e-09 + Linear kinetic energy = 9.98032e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 458.982, 540.2 + Mass transfer phase change = 6.87086e-10 + D10, D32, Dmax (mu) = 46.4923, 68.6084, 183.68 + Liquid penetration 95% mass (m) = 0.0138866 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00981189, Final residual = 5.34848e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0387078, Final residual = 1.34138e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000512158, Final residual = 3.46573e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00031563, Final residual = 2.26453e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000409696, Final residual = 3.18632e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000409683, Final residual = 3.1952e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000535438, Final residual = 3.11751e-08, No Iterations 1 +min/max(T) = 807.34, 2746.9 +GAMG: Solving for p, Initial residual = 0.019357, Final residual = 8.04522e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.90685e-05, global = 1.85706e-05, cumulative = 0.0157246 +GAMG: Solving for p, Initial residual = 7.76581e-05, Final residual = 7.5407e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.86359e-05, global = 1.86314e-05, cumulative = 0.0157433 +smoothSolver: Solving for epsilon, Initial residual = 0.000653935, Final residual = 7.64785e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000653335, Final residual = 1.12568e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.077806 s +other Time = 0 s +rho Equations = 0.000172 s +U Equations = 0.001032 s +Y Equations = 0.0022081 s +E Equations = 0.000492 s +p Equations = 0.001927 s +calculate parcels = 214.13 s +chemistry correctThermo = 0.001973 s +turbulence correct = 0.000944 s +combustion correct(in Y) = 0.0688769 s +percentage of chemistry = 88.5239 % +percentage of rho/U/Y/E = 5.01774 % +========Time details of each equation======= +rhoEqn Time = 0.0003 s +rhoEqn assamble = 0.000238 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001031 s +UEqn assamble = 0.000614 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000417 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001652 s +YEqn assamble = 0.000549 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000163 s +YEqn correct boundary = 0 s +EEqn Time = 0.000366 s +EEqn assamble = 0.000275 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.1e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 302.21 s ClockTime = 303 s +Courant Number mean: 0.00420154 max: 0.016207 +Time = 0.0022225 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21719 + Current mass in system = 1.01744e-09 + Linear momentum = (1.4386e-11 -4.25296e-09 0) + |Linear momentum| = 4.25298e-09 + Linear kinetic energy = 9.95436e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 459.152, 540.2 + Mass transfer phase change = 6.88704e-10 + D10, D32, Dmax (mu) = 46.458, 68.5588, 183.548 + Liquid penetration 95% mass (m) = 0.013894 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0104068, Final residual = 5.48479e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0404329, Final residual = 1.37496e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000510249, Final residual = 3.43675e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00031015, Final residual = 2.17061e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000403281, Final residual = 3.07778e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000403264, Final residual = 3.08651e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000528606, Final residual = 3.05286e-08, No Iterations 1 +min/max(T) = 807.324, 2746.72 +GAMG: Solving for p, Initial residual = 0.0181459, Final residual = 7.15675e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.9071e-05, global = 1.85989e-05, cumulative = 0.0157619 +GAMG: Solving for p, Initial residual = 6.89844e-05, Final residual = 6.08507e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.86625e-05, global = 1.86587e-05, cumulative = 0.0157805 +smoothSolver: Solving for epsilon, Initial residual = 0.000650427, Final residual = 7.55861e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000649761, Final residual = 1.10581e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.10291 s +other Time = 0 s +rho Equations = 0.000204 s +U Equations = 0.001186 s +Y Equations = 0.00215111 s +E Equations = 0.000488 s +p Equations = 0.001759 s +calculate parcels = 214.449 s +chemistry correctThermo = 0.002083 s +turbulence correct = 0.000926 s +combustion correct(in Y) = 0.0939109 s +percentage of chemistry = 91.2554 % +percentage of rho/U/Y/E = 3.91518 % +========Time details of each equation======= +rhoEqn Time = 0.000323 s +rhoEqn assamble = 0.000262 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001185 s +UEqn assamble = 0.000687 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000498 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001528 s +YEqn assamble = 0.000547 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000131 s +YEqn correct boundary = 0 s +EEqn Time = 0.000364 s +EEqn assamble = 0.000272 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 302.63 s ClockTime = 303 s +Courant Number mean: 0.0040492 max: 0.0159908 +Time = 0.002225 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21719 + Current mass in system = 1.01582e-09 + Linear momentum = (1.4601e-11 -4.24437e-09 0) + |Linear momentum| = 4.2444e-09 + Linear kinetic energy = 9.92834e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 459.321, 540.2 + Mass transfer phase change = 6.90322e-10 + D10, D32, Dmax (mu) = 46.392, 68.5074, 183.416 + Liquid penetration 95% mass (m) = 0.0139026 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.010821, Final residual = 5.53314e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0421567, Final residual = 1.40594e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000508361, Final residual = 3.39044e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000304565, Final residual = 2.07819e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000396826, Final residual = 2.97017e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000396816, Final residual = 2.97865e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000521032, Final residual = 2.98038e-08, No Iterations 1 +min/max(T) = 807.306, 2746.56 +GAMG: Solving for p, Initial residual = 0.0170087, Final residual = 6.53647e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.90421e-05, global = 1.85741e-05, cumulative = 0.0157991 +GAMG: Solving for p, Initial residual = 6.22053e-05, Final residual = 5.70662e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.86421e-05, global = 1.86384e-05, cumulative = 0.0158177 +smoothSolver: Solving for epsilon, Initial residual = 0.000646727, Final residual = 7.47224e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000646314, Final residual = 1.0867e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100126 s +other Time = 0 s +rho Equations = 0.000182 s +U Equations = 0.001287 s +Y Equations = 0.00245621 s +E Equations = 0.000587 s +p Equations = 0.001983 s +calculate parcels = 214.791 s +chemistry correctThermo = 0.002896 s +turbulence correct = 0.000977 s +combustion correct(in Y) = 0.0895588 s +percentage of chemistry = 89.4461 % +percentage of rho/U/Y/E = 4.50653 % +========Time details of each equation======= +rhoEqn Time = 0.00032 s +rhoEqn assamble = 0.000253 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001286 s +UEqn assamble = 0.000779 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000507 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00183 s +YEqn assamble = 0.000643 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000206 s +YEqn correct boundary = 0 s +EEqn Time = 0.000432 s +EEqn assamble = 0.00032 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 303.07 s ClockTime = 304 s +Courant Number mean: 0.00389374 max: 0.0156797 +Time = 0.0022275 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21716 + Current mass in system = 1.01414e-09 + Linear momentum = (1.47926e-11 -4.23569e-09 0) + |Linear momentum| = 4.23571e-09 + Linear kinetic energy = 9.90217e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 459.491, 540.2 + Mass transfer phase change = 6.92002e-10 + D10, D32, Dmax (mu) = 46.3579, 68.4637, 183.285 + Liquid penetration 95% mass (m) = 0.013911 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0108925, Final residual = 5.53465e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0438947, Final residual = 1.4346e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000525765, Final residual = 3.65269e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000299545, Final residual = 2.00077e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000393453, Final residual = 2.93936e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000393446, Final residual = 2.94848e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000514606, Final residual = 2.97361e-08, No Iterations 1 +min/max(T) = 807.29, 2746.43 +GAMG: Solving for p, Initial residual = 0.016125, Final residual = 0.000149733, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.01307e-05, global = 1.91788e-05, cumulative = 0.0158369 +GAMG: Solving for p, Initial residual = 0.000143784, Final residual = 6.4829e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.93758e-05, global = 1.93713e-05, cumulative = 0.0158563 +smoothSolver: Solving for epsilon, Initial residual = 0.000651069, Final residual = 7.53564e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000648141, Final residual = 1.08301e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.108619 s +other Time = 0 s +rho Equations = 0.000157 s +U Equations = 0.001068 s +Y Equations = 0.00212485 s +E Equations = 0.000482 s +p Equations = 0.002002 s +calculate parcels = 215.147 s +chemistry correctThermo = 0.002062 s +turbulence correct = 0.000822 s +combustion correct(in Y) = 0.0996921 s +percentage of chemistry = 91.7815 % +percentage of rho/U/Y/E = 3.52779 % +========Time details of each equation======= +rhoEqn Time = 0.000309 s +rhoEqn assamble = 0.000239 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001067 s +UEqn assamble = 0.000643 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000424 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001556 s +YEqn assamble = 0.000571 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000139 s +YEqn correct boundary = 0 s +EEqn Time = 0.000363 s +EEqn assamble = 0.000271 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 303.54 s ClockTime = 304 s +Courant Number mean: 0.00373905 max: 0.0153591 +Time = 0.00223 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21715 + Current mass in system = 1.01252e-09 + Linear momentum = (1.49695e-11 -4.22701e-09 0) + |Linear momentum| = 4.22703e-09 + Linear kinetic energy = 9.87591e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 459.66, 540.2 + Mass transfer phase change = 6.93623e-10 + D10, D32, Dmax (mu) = 46.3006, 68.4125, 183.153 + Liquid penetration 95% mass (m) = 0.013918 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0155068, Final residual = 8.05342e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0460061, Final residual = 1.47985e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000508657, Final residual = 3.31613e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000292554, Final residual = 1.92577e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000382177, Final residual = 2.77599e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000382166, Final residual = 2.78462e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000507625, Final residual = 2.85115e-08, No Iterations 1 +min/max(T) = 807.277, 2746.1 +GAMG: Solving for p, Initial residual = 0.0156859, Final residual = 0.000193969, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.95206e-05, global = 1.86652e-05, cumulative = 0.015875 +GAMG: Solving for p, Initial residual = 0.000188747, Final residual = 8.73542e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.86852e-05, global = 1.8682e-05, cumulative = 0.0158936 +smoothSolver: Solving for epsilon, Initial residual = 0.000636536, Final residual = 7.25792e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000638908, Final residual = 1.04909e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.114482 s +other Time = 1e-06 s +rho Equations = 0.000247 s +U Equations = 0.001912 s +Y Equations = 0.00264298 s +E Equations = 0.000603 s +p Equations = 0.002283 s +calculate parcels = 215.481 s +chemistry correctThermo = 0.0029 s +turbulence correct = 0.001009 s +combustion correct(in Y) = 0.102575 s +percentage of chemistry = 89.5993 % +percentage of rho/U/Y/E = 4.72125 % +========Time details of each equation======= +rhoEqn Time = 0.000403 s +rhoEqn assamble = 0.000304 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001911 s +UEqn assamble = 0.001097 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000814 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001567 s +YEqn assamble = 0.000633 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = -4.2e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000442 s +EEqn assamble = 0.000329 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 303.99 s ClockTime = 305 s +Courant Number mean: 0.003578 max: 0.0149448 +Time = 0.0022325 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21714 + Current mass in system = 1.0109e-09 + Linear momentum = (1.51255e-11 -4.21828e-09 0) + |Linear momentum| = 4.2183e-09 + Linear kinetic energy = 9.8495e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 459.828, 540.2 + Mass transfer phase change = 6.95247e-10 + D10, D32, Dmax (mu) = 46.2429, 68.3605, 183.023 + Liquid penetration 95% mass (m) = 0.0139257 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0151772, Final residual = 7.61651e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0476485, Final residual = 1.49548e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000506546, Final residual = 3.28195e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000287351, Final residual = 1.84952e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000376201, Final residual = 2.68869e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000376185, Final residual = 2.69703e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000499694, Final residual = 2.7768e-08, No Iterations 1 +min/max(T) = 807.264, 2745.91 +GAMG: Solving for p, Initial residual = 0.01434, Final residual = 0.000129946, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.95281e-05, global = 1.86459e-05, cumulative = 0.0159123 +GAMG: Solving for p, Initial residual = 0.000124976, Final residual = 3.28981e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.87156e-05, global = 1.87136e-05, cumulative = 0.015931 +smoothSolver: Solving for epsilon, Initial residual = 0.000634632, Final residual = 7.19095e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000637617, Final residual = 1.0318e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.107276 s +other Time = 0 s +rho Equations = 0.000181 s +U Equations = 0.001284 s +Y Equations = 0.00258157 s +E Equations = 0.000612 s +p Equations = 0.00226 s +calculate parcels = 215.819 s +chemistry correctThermo = 0.003012 s +turbulence correct = 0.00088 s +combustion correct(in Y) = 0.0962544 s +percentage of chemistry = 89.726 % +percentage of rho/U/Y/E = 4.3426 % +========Time details of each equation======= +rhoEqn Time = 0.000328 s +rhoEqn assamble = 0.000258 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001283 s +UEqn assamble = 0.000786 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000497 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001931 s +YEqn assamble = 0.000675 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000192 s +YEqn correct boundary = 0 s +EEqn Time = 0.000449 s +EEqn assamble = 0.000338 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 304.43 s ClockTime = 305 s +Courant Number mean: 0.00341317 max: 0.0145884 +Time = 0.002235 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21713 + Current mass in system = 1.00923e-09 + Linear momentum = (1.52293e-11 -4.20949e-09 0) + |Linear momentum| = 4.20951e-09 + Linear kinetic energy = 9.82292e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 459.997, 540.2 + Mass transfer phase change = 6.96917e-10 + D10, D32, Dmax (mu) = 46.177, 68.3111, 182.891 + Liquid penetration 95% mass (m) = 0.0139325 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0131107, Final residual = 6.21516e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0494164, Final residual = 1.51811e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000520743, Final residual = 3.46297e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000283279, Final residual = 1.78145e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000375074, Final residual = 2.66148e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000375054, Final residual = 2.66992e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000491013, Final residual = 2.746e-08, No Iterations 1 +min/max(T) = 807.252, 2745.89 +GAMG: Solving for p, Initial residual = 0.0132186, Final residual = 0.000158494, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.02178e-05, global = 1.90859e-05, cumulative = 0.0159501 +GAMG: Solving for p, Initial residual = 0.000150101, Final residual = 9.03268e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.92607e-05, global = 1.92542e-05, cumulative = 0.0159693 +smoothSolver: Solving for epsilon, Initial residual = 0.000639497, Final residual = 7.267e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000639425, Final residual = 1.02766e-07, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.088542 s +other Time = 0 s +rho Equations = 0.000171 s +U Equations = 0.00104 s +Y Equations = 0.00243295 s +E Equations = 0.000601 s +p Equations = 0.002414 s +calculate parcels = 216.074 s +chemistry correctThermo = 0.003063 s +turbulence correct = 0.001046 s +combustion correct(in Y) = 0.0775651 s +percentage of chemistry = 87.6026 % +percentage of rho/U/Y/E = 4.79428 % +========Time details of each equation======= +rhoEqn Time = 0.000331 s +rhoEqn assamble = 0.000261 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00104 s +UEqn assamble = 0.000612 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000428 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001856 s +YEqn assamble = 0.000631 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000208 s +YEqn correct boundary = 0 s +EEqn Time = 0.00044 s +EEqn assamble = 0.000328 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000112 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 304.77 s ClockTime = 305 s +Courant Number mean: 0.00324945 max: 0.01419 +Time = 0.0022375 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21712 + Current mass in system = 1.0076e-09 + Linear momentum = (1.53137e-11 -4.20068e-09 0) + |Linear momentum| = 4.2007e-09 + Linear kinetic energy = 9.79624e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 460.166, 540.2 + Mass transfer phase change = 6.9854e-10 + D10, D32, Dmax (mu) = 46.1156, 68.2593, 182.76 + Liquid penetration 95% mass (m) = 0.0139399 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0149516, Final residual = 7.70722e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0513397, Final residual = 1.54195e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000500338, Final residual = 3.16422e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000277709, Final residual = 1.72209e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000364473, Final residual = 2.52042e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000364453, Final residual = 2.52872e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000480206, Final residual = 2.62076e-08, No Iterations 1 +min/max(T) = 807.239, 2745.69 +GAMG: Solving for p, Initial residual = 0.0126051, Final residual = 0.000173455, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.94934e-05, global = 1.87106e-05, cumulative = 0.0159881 +GAMG: Solving for p, Initial residual = 0.000171157, Final residual = 9.72655e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.87034e-05, global = 1.86999e-05, cumulative = 0.0160068 +smoothSolver: Solving for epsilon, Initial residual = 0.000624735, Final residual = 6.9995e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000630437, Final residual = 9.9716e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.092673 s +other Time = 1e-06 s +rho Equations = 0.000152 s +U Equations = 0.001013 s +Y Equations = 0.00211492 s +E Equations = 0.000496 s +p Equations = 0.002348 s +calculate parcels = 216.43 s +chemistry correctThermo = 0.002429 s +turbulence correct = 0.001012 s +combustion correct(in Y) = 0.0829281 s +percentage of chemistry = 89.4846 % +percentage of rho/U/Y/E = 4.07445 % +========Time details of each equation======= +rhoEqn Time = 0.000306 s +rhoEqn assamble = 0.000241 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001013 s +UEqn assamble = 0.000589 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000424 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001553 s +YEqn assamble = 0.00054 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.00014 s +YEqn correct boundary = 0 s +EEqn Time = 0.000373 s +EEqn assamble = 0.00028 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 305.22 s ClockTime = 306 s +Courant Number mean: 0.00308184 max: 0.0138197 +Time = 0.00224 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21710 + Current mass in system = 1.00598e-09 + Linear momentum = (1.53748e-11 -4.19184e-09 0) + |Linear momentum| = 4.19187e-09 + Linear kinetic energy = 9.76946e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 460.336, 540.2 + Mass transfer phase change = 7.00164e-10 + D10, D32, Dmax (mu) = 46.0769, 68.2076, 182.628 + Liquid penetration 95% mass (m) = 0.0139479 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0129224, Final residual = 6.28221e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0531421, Final residual = 1.55463e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000501347, Final residual = 3.15831e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000273529, Final residual = 1.66252e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000359945, Final residual = 2.46307e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000359914, Final residual = 2.4714e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000472688, Final residual = 2.56545e-08, No Iterations 1 +min/max(T) = 807.226, 2745.61 +GAMG: Solving for p, Initial residual = 0.01144, Final residual = 0.000110149, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.94665e-05, global = 1.8673e-05, cumulative = 0.0160254 +GAMG: Solving for p, Initial residual = 0.000106811, Final residual = 2.90206e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.8724e-05, global = 1.87224e-05, cumulative = 0.0160441 +smoothSolver: Solving for epsilon, Initial residual = 0.000622963, Final residual = 6.94333e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000628798, Final residual = 9.81974e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.118811 s +other Time = 1e-06 s +rho Equations = 0.000179 s +U Equations = 0.001206 s +Y Equations = 0.00251482 s +E Equations = 0.000606 s +p Equations = 0.002597 s +calculate parcels = 216.783 s +chemistry correctThermo = 0.002918 s +turbulence correct = 0.00101 s +combustion correct(in Y) = 0.107502 s +percentage of chemistry = 90.4817 % +percentage of rho/U/Y/E = 3.79243 % +========Time details of each equation======= +rhoEqn Time = 0.000356 s +rhoEqn assamble = 0.000272 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001204 s +UEqn assamble = 0.000687 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000517 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001865 s +YEqn assamble = 0.000648 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000185 s +YEqn correct boundary = 0 s +EEqn Time = 0.000446 s +EEqn assamble = 0.000335 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 305.7 s ClockTime = 306 s +Courant Number mean: 0.00291271 max: 0.0135025 +Time = 0.0022425 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21708 + Current mass in system = 1.00435e-09 + Linear momentum = (1.5434e-11 -4.18297e-09 0) + |Linear momentum| = 4.18299e-09 + Linear kinetic energy = 9.74258e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 460.507, 540.2 + Mass transfer phase change = 7.01798e-10 + D10, D32, Dmax (mu) = 46.0309, 68.1574, 182.496 + Liquid penetration 95% mass (m) = 0.0139569 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0111559, Final residual = 5.30529e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0551364, Final residual = 1.5718e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.0004962, Final residual = 3.12449e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000270414, Final residual = 1.61555e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000355713, Final residual = 2.40722e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000355681, Final residual = 2.41542e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00046172, Final residual = 2.49279e-08, No Iterations 1 +min/max(T) = 807.211, 2745.66 +GAMG: Solving for p, Initial residual = 0.010283, Final residual = 9.2094e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.94091e-05, global = 1.87451e-05, cumulative = 0.0160629 +GAMG: Solving for p, Initial residual = 8.80922e-05, Final residual = 2.46824e-07, No Iterations 3 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.88279e-05, global = 1.88263e-05, cumulative = 0.0160817 +smoothSolver: Solving for epsilon, Initial residual = 0.000622081, Final residual = 6.89945e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000627917, Final residual = 9.68441e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.114791 s +other Time = 1e-06 s +rho Equations = 0.000195 s +U Equations = 0.001281 s +Y Equations = 0.00209388 s +E Equations = 0.000526 s +p Equations = 0.001848 s +calculate parcels = 217.112 s +chemistry correctThermo = 0.002269 s +turbulence correct = 0.000991 s +combustion correct(in Y) = 0.105368 s +percentage of chemistry = 91.7913 % +percentage of rho/U/Y/E = 3.56812 % +========Time details of each equation======= +rhoEqn Time = 0.000313 s +rhoEqn assamble = 0.000247 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001281 s +UEqn assamble = 0.000778 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000503 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00144 s +YEqn assamble = 0.000515 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.5e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.00038 s +EEqn assamble = 0.000281 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.9e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 306.14 s ClockTime = 307 s +Courant Number mean: 0.00274297 max: 0.0132557 +Time = 0.002245 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21707 + Current mass in system = 1.00272e-09 + Linear momentum = (1.54968e-11 -4.17409e-09 0) + |Linear momentum| = 4.17412e-09 + Linear kinetic energy = 9.71565e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 460.679, 540.2 + Mass transfer phase change = 7.03422e-10 + D10, D32, Dmax (mu) = 45.9719, 68.1048, 182.363 + Liquid penetration 95% mass (m) = 0.0139652 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00987909, Final residual = 4.4613e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0571122, Final residual = 1.58186e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00049872, Final residual = 3.10668e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000266253, Final residual = 1.56403e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000351789, Final residual = 2.35286e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000351754, Final residual = 2.36095e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000452137, Final residual = 2.42444e-08, No Iterations 1 +min/max(T) = 807.196, 2745.71 +GAMG: Solving for p, Initial residual = 0.00939532, Final residual = 7.60445e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.92864e-05, global = 1.86545e-05, cumulative = 0.0161004 +GAMG: Solving for p, Initial residual = 7.34442e-05, Final residual = 8.15156e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.87318e-05, global = 1.87255e-05, cumulative = 0.0161191 +smoothSolver: Solving for epsilon, Initial residual = 0.000618219, Final residual = 6.81962e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000624357, Final residual = 9.52634e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.09911 s +other Time = 0 s +rho Equations = 0.000186 s +U Equations = 0.001207 s +Y Equations = 0.00221849 s +E Equations = 0.000492 s +p Equations = 0.001719 s +calculate parcels = 217.462 s +chemistry correctThermo = 0.00209 s +turbulence correct = 0.000869 s +combustion correct(in Y) = 0.0901125 s +percentage of chemistry = 90.9217 % +percentage of rho/U/Y/E = 4.14034 % +========Time details of each equation======= +rhoEqn Time = 0.000304 s +rhoEqn assamble = 0.000239 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001207 s +UEqn assamble = 0.000696 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000511 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001552 s +YEqn assamble = 0.000555 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000115 s +YEqn correct boundary = 0 s +EEqn Time = 0.000371 s +EEqn assamble = 0.000279 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 306.59 s ClockTime = 307 s +Courant Number mean: 0.0025723 max: 0.0130988 +Time = 0.0022475 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21705 + Current mass in system = 1.00109e-09 + Linear momentum = (1.55593e-11 -4.1652e-09 0) + |Linear momentum| = 4.16523e-09 + Linear kinetic energy = 9.68864e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 460.853, 540.2 + Mass transfer phase change = 7.05048e-10 + D10, D32, Dmax (mu) = 45.9274, 68.0526, 182.229 + Liquid penetration 95% mass (m) = 0.0139748 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0092592, Final residual = 3.9053e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0592039, Final residual = 1.59379e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000496888, Final residual = 3.07965e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000262438, Final residual = 1.51916e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000347363, Final residual = 2.29988e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000347348, Final residual = 2.30772e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000442468, Final residual = 2.36182e-08, No Iterations 1 +min/max(T) = 807.181, 2745.71 +GAMG: Solving for p, Initial residual = 0.0085393, Final residual = 6.82983e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.92144e-05, global = 1.86401e-05, cumulative = 0.0161377 +GAMG: Solving for p, Initial residual = 6.6453e-05, Final residual = 6.29679e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.87414e-05, global = 1.87368e-05, cumulative = 0.0161565 +smoothSolver: Solving for epsilon, Initial residual = 0.000614787, Final residual = 6.7512e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000621651, Final residual = 9.38703e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.081849 s +other Time = 0 s +rho Equations = 0.000172 s +U Equations = 0.001089 s +Y Equations = 0.00228037 s +E Equations = 0.000535 s +p Equations = 0.001847 s +calculate parcels = 217.784 s +chemistry correctThermo = 0.002072 s +turbulence correct = 0.00095 s +combustion correct(in Y) = 0.0726346 s +percentage of chemistry = 88.7422 % +percentage of rho/U/Y/E = 4.98035 % +========Time details of each equation======= +rhoEqn Time = 0.000298 s +rhoEqn assamble = 0.000239 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001088 s +UEqn assamble = 0.000647 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000441 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001626 s +YEqn assamble = 0.000569 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 9.5e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000388 s +EEqn assamble = 0.000292 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 306.99 s ClockTime = 308 s +Courant Number mean: 0.00240111 max: 0.0130677 +Time = 0.00225 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21701 + Current mass in system = 9.99466e-10 + Linear momentum = (1.56187e-11 -4.15627e-09 0) + |Linear momentum| = 4.1563e-09 + Linear kinetic energy = 9.66153e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 461.027, 540.2 + Mass transfer phase change = 7.06677e-10 + D10, D32, Dmax (mu) = 45.921, 68.0015, 182.096 + Liquid penetration 95% mass (m) = 0.0139848 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00911598, Final residual = 3.4566e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0613426, Final residual = 1.60509e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000495949, Final residual = 3.05359e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000259007, Final residual = 1.4819e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000343353, Final residual = 2.2502e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000343342, Final residual = 2.25804e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000432961, Final residual = 2.30006e-08, No Iterations 1 +min/max(T) = 807.169, 2745.7 +GAMG: Solving for p, Initial residual = 0.00779027, Final residual = 6.34043e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.92152e-05, global = 1.86549e-05, cumulative = 0.0161751 +GAMG: Solving for p, Initial residual = 6.18466e-05, Final residual = 7.36055e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.87775e-05, global = 1.87719e-05, cumulative = 0.0161939 +smoothSolver: Solving for epsilon, Initial residual = 0.000610522, Final residual = 6.67921e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000618796, Final residual = 9.24641e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.108832 s +other Time = 0 s +rho Equations = 0.00016 s +U Equations = 0.001034 s +Y Equations = 0.00242638 s +E Equations = 0.000603 s +p Equations = 0.002159 s +calculate parcels = 218.063 s +chemistry correctThermo = 0.002901 s +turbulence correct = 0.001107 s +combustion correct(in Y) = 0.0982526 s +percentage of chemistry = 90.2792 % +percentage of rho/U/Y/E = 3.88064 % +========Time details of each equation======= +rhoEqn Time = 0.000306 s +rhoEqn assamble = 0.00024 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.6e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001033 s +UEqn assamble = 0.000583 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00045 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00186 s +YEqn assamble = 0.000641 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000231 s +YEqn correct boundary = 0 s +EEqn Time = 0.000442 s +EEqn assamble = 0.000329 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 307.38 s ClockTime = 308 s +Courant Number mean: 0.00222988 max: 0.0130399 +Time = 0.0022525 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21699 + Current mass in system = 9.97838e-10 + Linear momentum = (1.56703e-11 -4.14731e-09 0) + |Linear momentum| = 4.14734e-09 + Linear kinetic energy = 9.6343e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 461.202, 540.2 + Mass transfer phase change = 7.08304e-10 + D10, D32, Dmax (mu) = 45.8935, 67.9489, 181.962 + Liquid penetration 95% mass (m) = 0.0139936 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00876971, Final residual = 3.16603e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0635348, Final residual = 1.61598e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000493769, Final residual = 3.00939e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000255403, Final residual = 1.44897e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000339826, Final residual = 2.20974e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00033985, Final residual = 2.21747e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000424019, Final residual = 2.24835e-08, No Iterations 1 +min/max(T) = 807.159, 2745.67 +GAMG: Solving for p, Initial residual = 0.00712413, Final residual = 5.56619e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.91591e-05, global = 1.86292e-05, cumulative = 0.0162125 +GAMG: Solving for p, Initial residual = 5.44692e-05, Final residual = 5.7519e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.87649e-05, global = 1.87602e-05, cumulative = 0.0162313 +smoothSolver: Solving for epsilon, Initial residual = 0.00060591, Final residual = 6.60082e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000616063, Final residual = 9.10843e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.104372 s +other Time = 0 s +rho Equations = 0.000181 s +U Equations = 0.001211 s +Y Equations = 0.00246365 s +E Equations = 0.000597 s +p Equations = 0.002122 s +calculate parcels = 218.395 s +chemistry correctThermo = 0.002922 s +turbulence correct = 0.00104 s +combustion correct(in Y) = 0.0936334 s +percentage of chemistry = 89.7112 % +percentage of rho/U/Y/E = 4.26613 % +========Time details of each equation======= +rhoEqn Time = 0.000331 s +rhoEqn assamble = 0.000263 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00121 s +UEqn assamble = 0.000715 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000495 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001822 s +YEqn assamble = 0.000638 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000189 s +YEqn correct boundary = 0 s +EEqn Time = 0.00044 s +EEqn assamble = 0.000327 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 307.82 s ClockTime = 308 s +Courant Number mean: 0.00205945 max: 0.0130175 +Time = 0.002255 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21699 + Current mass in system = 9.9621e-10 + Linear momentum = (1.57101e-11 -4.1383e-09 0) + |Linear momentum| = 4.13833e-09 + Linear kinetic energy = 9.60689e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 461.378, 540.2 + Mass transfer phase change = 7.09933e-10 + D10, D32, Dmax (mu) = 45.8243, 67.8946, 181.828 + Liquid penetration 95% mass (m) = 0.0140014 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00886735, Final residual = 3.17977e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0657566, Final residual = 1.62685e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000491248, Final residual = 2.97366e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000251651, Final residual = 1.41746e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000336109, Final residual = 2.1639e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000336137, Final residual = 2.17162e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000414814, Final residual = 2.19261e-08, No Iterations 1 +min/max(T) = 807.148, 2745.65 +GAMG: Solving for p, Initial residual = 0.00669344, Final residual = 4.95032e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.91338e-05, global = 1.86288e-05, cumulative = 0.0162499 +GAMG: Solving for p, Initial residual = 4.85452e-05, Final residual = 4.51108e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.87708e-05, global = 1.87669e-05, cumulative = 0.0162687 +smoothSolver: Solving for epsilon, Initial residual = 0.000601205, Final residual = 6.52175e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000613141, Final residual = 8.97301e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.113093 s +other Time = 1e-06 s +rho Equations = 0.000224 s +U Equations = 0.001322 s +Y Equations = 0.00248215 s +E Equations = 0.000613 s +p Equations = 0.002377 s +calculate parcels = 218.764 s +chemistry correctThermo = 0.002921 s +turbulence correct = 0.001077 s +combustion correct(in Y) = 0.101856 s +percentage of chemistry = 90.0638 % +percentage of rho/U/Y/E = 4.10383 % +========Time details of each equation======= +rhoEqn Time = 0.000406 s +rhoEqn assamble = 0.000305 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.000101 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001322 s +UEqn assamble = 0.000817 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000505 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001821 s +YEqn assamble = 0.000645 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000182 s +YEqn correct boundary = 0 s +EEqn Time = 0.000455 s +EEqn assamble = 0.000329 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000126 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 308.3 s ClockTime = 309 s +Courant Number mean: 0.00190978 max: 0.0129958 +Time = 0.0022575 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21695 + Current mass in system = 9.94566e-10 + Linear momentum = (1.57293e-11 -4.12919e-09 0) + |Linear momentum| = 4.12922e-09 + Linear kinetic energy = 9.57922e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 461.554, 540.2 + Mass transfer phase change = 7.11577e-10 + D10, D32, Dmax (mu) = 45.8052, 67.8435, 181.693 + Liquid penetration 95% mass (m) = 0.0140092 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.00907135, Final residual = 3.2985e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0679951, Final residual = 1.63871e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000487434, Final residual = 2.94054e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000247783, Final residual = 1.38679e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000331162, Final residual = 2.11227e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.0003312, Final residual = 2.1202e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000407954, Final residual = 2.14446e-08, No Iterations 1 +min/max(T) = 807.14, 2745.62 +GAMG: Solving for p, Initial residual = 0.00651004, Final residual = 5.37174e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.92768e-05, global = 1.88092e-05, cumulative = 0.0162875 +GAMG: Solving for p, Initial residual = 5.27085e-05, Final residual = 5.94292e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.89555e-05, global = 1.89517e-05, cumulative = 0.0163065 +smoothSolver: Solving for epsilon, Initial residual = 0.000596902, Final residual = 6.45849e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000610791, Final residual = 8.86368e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.11153 s +other Time = 1e-06 s +rho Equations = 0.000156 s +U Equations = 0.001069 s +Y Equations = 0.00371259 s +E Equations = 0.000985 s +p Equations = 0.003862 s +calculate parcels = 219.118 s +chemistry correctThermo = 0.005642 s +turbulence correct = 0.001869 s +combustion correct(in Y) = 0.0940054 s +percentage of chemistry = 84.2871 % +percentage of rho/U/Y/E = 5.31031 % +========Time details of each equation======= +rhoEqn Time = 0.00049 s +rhoEqn assamble = 0.00037 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.00012 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001068 s +UEqn assamble = 0.00063 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000438 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.003152 s +YEqn assamble = 0.001065 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000625 s +YEqn correct boundary = 0 s +EEqn Time = 0.000732 s +EEqn assamble = 0.000535 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000197 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 308.76 s ClockTime = 309 s +Courant Number mean: 0.0017812 max: 0.0130147 +Time = 0.00226 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21694 + Current mass in system = 9.9293e-10 + Linear momentum = (1.57376e-11 -4.12003e-09 0) + |Linear momentum| = 4.12006e-09 + Linear kinetic energy = 9.55136e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 461.732, 540.2 + Mass transfer phase change = 7.13213e-10 + D10, D32, Dmax (mu) = 45.7453, 67.7886, 181.558 + Liquid penetration 95% mass (m) = 0.0140177 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0100151, Final residual = 3.91495e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0702622, Final residual = 1.65229e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000488162, Final residual = 2.90501e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000243792, Final residual = 1.35614e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000327955, Final residual = 2.07198e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000327991, Final residual = 2.07969e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000405288, Final residual = 2.10902e-08, No Iterations 1 +min/max(T) = 807.135, 2745.57 +GAMG: Solving for p, Initial residual = 0.00653231, Final residual = 5.82081e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.92623e-05, global = 1.87278e-05, cumulative = 0.0163252 +GAMG: Solving for p, Initial residual = 5.68372e-05, Final residual = 7.36216e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.88591e-05, global = 1.88539e-05, cumulative = 0.016344 +smoothSolver: Solving for epsilon, Initial residual = 0.000590855, Final residual = 6.35533e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000606707, Final residual = 8.71624e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.106666 s +other Time = 0 s +rho Equations = 0.000192 s +U Equations = 0.001195 s +Y Equations = 0.00247794 s +E Equations = 0.000611 s +p Equations = 0.002088 s +calculate parcels = 219.477 s +chemistry correctThermo = 0.002905 s +turbulence correct = 0.000984 s +combustion correct(in Y) = 0.0959491 s +percentage of chemistry = 89.9528 % +percentage of rho/U/Y/E = 4.19622 % +========Time details of each equation======= +rhoEqn Time = 0.00036 s +rhoEqn assamble = 0.00026 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 0.0001 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001194 s +UEqn assamble = 0.000697 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000497 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001816 s +YEqn assamble = 0.000646 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000178 s +YEqn correct boundary = 0 s +EEqn Time = 0.000453 s +EEqn assamble = 0.00034 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 309.23 s ClockTime = 310 s +Courant Number mean: 0.00166871 max: 0.0129786 +Time = 0.0022625 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21691 + Current mass in system = 9.91282e-10 + Linear momentum = (1.57366e-11 -4.11077e-09 0) + |Linear momentum| = 4.1108e-09 + Linear kinetic energy = 9.52318e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 461.91, 540.2 + Mass transfer phase change = 7.14861e-10 + D10, D32, Dmax (mu) = 45.7021, 67.7347, 181.423 + Liquid penetration 95% mass (m) = 0.0140245 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0101769, Final residual = 3.93256e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0724955, Final residual = 1.66823e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00048161, Final residual = 2.81105e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000239701, Final residual = 1.3238e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000322598, Final residual = 2.01467e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000322633, Final residual = 2.02223e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000402697, Final residual = 2.0653e-08, No Iterations 1 +min/max(T) = 807.132, 2745.52 +GAMG: Solving for p, Initial residual = 0.00663779, Final residual = 5.48616e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.9347e-05, global = 1.88549e-05, cumulative = 0.0163629 +GAMG: Solving for p, Initial residual = 5.37665e-05, Final residual = 6.75983e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.89948e-05, global = 1.89898e-05, cumulative = 0.0163819 +smoothSolver: Solving for epsilon, Initial residual = 0.000586217, Final residual = 6.29429e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000604321, Final residual = 8.61871e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.078156 s +other Time = 0 s +rho Equations = 0.000165 s +U Equations = 0.001111 s +Y Equations = 0.00214676 s +E Equations = 0.000529 s +p Equations = 0.001735 s +calculate parcels = 219.758 s +chemistry correctThermo = 0.001949 s +turbulence correct = 0.000866 s +combustion correct(in Y) = 0.0694652 s +percentage of chemistry = 88.8802 % +percentage of rho/U/Y/E = 5.05625 % +========Time details of each equation======= +rhoEqn Time = 0.00029 s +rhoEqn assamble = 0.000231 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 5.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00111 s +UEqn assamble = 0.0007 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00041 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001581 s +YEqn assamble = 0.000531 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000137 s +YEqn correct boundary = 0 s +EEqn Time = 0.000405 s +EEqn assamble = 0.000309 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.6e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 309.59 s ClockTime = 310 s +Courant Number mean: 0.00157404 max: 0.0129484 +Time = 0.002265 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21687 + Current mass in system = 9.89634e-10 + Linear momentum = (1.57294e-11 -4.10143e-09 0) + |Linear momentum| = 4.10146e-09 + Linear kinetic energy = 9.49473e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 462.09, 540.2 + Mass transfer phase change = 7.16509e-10 + D10, D32, Dmax (mu) = 45.6874, 67.6802, 181.333 + Liquid penetration 95% mass (m) = 0.0140324 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0107408, Final residual = 4.30369e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0746593, Final residual = 1.68702e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000483292, Final residual = 2.81649e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000236005, Final residual = 1.29158e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000318946, Final residual = 1.97079e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000318982, Final residual = 1.97831e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000402585, Final residual = 2.03599e-08, No Iterations 1 +min/max(T) = 807.131, 2745.45 +GAMG: Solving for p, Initial residual = 0.0068347, Final residual = 5.67468e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.94096e-05, global = 1.88926e-05, cumulative = 0.0164008 +GAMG: Solving for p, Initial residual = 5.56832e-05, Final residual = 7.87496e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.90059e-05, global = 1.90001e-05, cumulative = 0.0164198 +smoothSolver: Solving for epsilon, Initial residual = 0.000579742, Final residual = 6.19054e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000600205, Final residual = 8.48201e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.100349 s +other Time = 0 s +rho Equations = 0.000189 s +U Equations = 0.001434 s +Y Equations = 0.00247975 s +E Equations = 0.000613 s +p Equations = 0.002054 s +calculate parcels = 220.113 s +chemistry correctThermo = 0.002932 s +turbulence correct = 0.001315 s +combustion correct(in Y) = 0.0891113 s +percentage of chemistry = 88.8013 % +percentage of rho/U/Y/E = 4.69935 % +========Time details of each equation======= +rhoEqn Time = 0.000333 s +rhoEqn assamble = 0.000263 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001433 s +UEqn assamble = 0.000873 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.00056 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001737 s +YEqn assamble = 0.000639 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000139 s +YEqn correct boundary = 0 s +EEqn Time = 0.000456 s +EEqn assamble = 0.00033 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000126 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 310.05 s ClockTime = 311 s +Courant Number mean: 0.00149761 max: 0.0129249 +Time = 0.0022675 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21682 + Current mass in system = 9.87976e-10 + Linear momentum = (1.57209e-11 -4.09199e-09 0) + |Linear momentum| = 4.09202e-09 + Linear kinetic energy = 9.46597e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 462.271, 540.2 + Mass transfer phase change = 7.18167e-10 + D10, D32, Dmax (mu) = 45.6693, 67.6256, 181.46 + Liquid penetration 95% mass (m) = 0.0140408 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0110298, Final residual = 4.23577e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0767096, Final residual = 1.70199e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000478927, Final residual = 2.75538e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00023199, Final residual = 1.26066e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00031443, Final residual = 1.92791e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000314479, Final residual = 1.93537e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000402654, Final residual = 2.00045e-08, No Iterations 1 +min/max(T) = 807.129, 2745.37 +GAMG: Solving for p, Initial residual = 0.00703159, Final residual = 5.00286e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.9419e-05, global = 1.901e-05, cumulative = 0.0164388 +GAMG: Solving for p, Initial residual = 4.94197e-05, Final residual = 6.37563e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.91122e-05, global = 1.9108e-05, cumulative = 0.0164579 +smoothSolver: Solving for epsilon, Initial residual = 0.000574132, Final residual = 6.11521e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000597161, Final residual = 8.38799e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.105554 s +other Time = 1e-06 s +rho Equations = 0.000222 s +U Equations = 0.001301 s +Y Equations = 0.00287846 s +E Equations = 0.000676 s +p Equations = 0.002258 s +calculate parcels = 220.483 s +chemistry correctThermo = 0.002876 s +turbulence correct = 0.001061 s +combustion correct(in Y) = 0.0940725 s +percentage of chemistry = 89.1227 % +percentage of rho/U/Y/E = 4.81029 % +========Time details of each equation======= +rhoEqn Time = 0.000383 s +rhoEqn assamble = 0.000294 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001301 s +UEqn assamble = 0.000733 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000568 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002171 s +YEqn assamble = 0.000751 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000203 s +YEqn correct boundary = 0 s +EEqn Time = 0.000508 s +EEqn assamble = 0.000389 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000119 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 310.52 s ClockTime = 311 s +Courant Number mean: 0.00144504 max: 0.0129396 +Time = 0.00227 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21679 + Current mass in system = 9.86319e-10 + Linear momentum = (1.5709e-11 -4.08248e-09 0) + |Linear momentum| = 4.08251e-09 + Linear kinetic energy = 9.43696e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 462.452, 540.2 + Mass transfer phase change = 7.19824e-10 + D10, D32, Dmax (mu) = 45.6201, 67.5683, 181.589 + Liquid penetration 95% mass (m) = 0.0140482 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0114031, Final residual = 4.27191e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0786894, Final residual = 1.72543e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000477113, Final residual = 2.71077e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000227896, Final residual = 1.22884e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00031039, Final residual = 1.88015e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000310438, Final residual = 1.88746e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000403288, Final residual = 1.97311e-08, No Iterations 1 +min/max(T) = 807.128, 2745.27 +GAMG: Solving for p, Initial residual = 0.00729942, Final residual = 4.74629e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.94324e-05, global = 1.90085e-05, cumulative = 0.0164769 +GAMG: Solving for p, Initial residual = 4.71706e-05, Final residual = 5.04986e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.91019e-05, global = 1.90982e-05, cumulative = 0.016496 +smoothSolver: Solving for epsilon, Initial residual = 0.000567859, Final residual = 6.01723e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000593357, Final residual = 8.27928e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.119296 s +other Time = 1e-06 s +rho Equations = 0.000213 s +U Equations = 0.001451 s +Y Equations = 0.00249942 s +E Equations = 0.000586 s +p Equations = 0.002451 s +calculate parcels = 220.842 s +chemistry correctThermo = 0.002944 s +turbulence correct = 0.001068 s +combustion correct(in Y) = 0.107619 s +percentage of chemistry = 90.2114 % +percentage of rho/U/Y/E = 3.98121 % +========Time details of each equation======= +rhoEqn Time = 0.000378 s +rhoEqn assamble = 0.000299 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001449 s +UEqn assamble = 0.000877 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000572 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00178 s +YEqn assamble = 0.000673 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000146 s +YEqn correct boundary = 0 s +EEqn Time = 0.000433 s +EEqn assamble = 0.000322 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000111 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 311 s ClockTime = 312 s +Courant Number mean: 0.00141495 max: 0.0128885 +Time = 0.0022725 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21673 + Current mass in system = 9.84649e-10 + Linear momentum = (1.56919e-11 -4.07285e-09 0) + |Linear momentum| = 4.07288e-09 + Linear kinetic energy = 9.40758e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 462.635, 540.2 + Mass transfer phase change = 7.21494e-10 + D10, D32, Dmax (mu) = 45.6189, 67.5124, 181.719 + Liquid penetration 95% mass (m) = 0.0140548 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0112829, Final residual = 4.2006e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0805816, Final residual = 1.75433e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000474822, Final residual = 2.67683e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00022366, Final residual = 1.19541e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000305461, Final residual = 1.83584e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000305507, Final residual = 1.84301e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000403996, Final residual = 1.9515e-08, No Iterations 1 +min/max(T) = 807.126, 2745.17 +GAMG: Solving for p, Initial residual = 0.00762559, Final residual = 4.93447e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.9541e-05, global = 1.9168e-05, cumulative = 0.0165152 +GAMG: Solving for p, Initial residual = 4.91341e-05, Final residual = 5.46321e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.92548e-05, global = 1.92514e-05, cumulative = 0.0165344 +smoothSolver: Solving for epsilon, Initial residual = 0.000561797, Final residual = 5.93273e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000589596, Final residual = 8.18953e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.098025 s +other Time = 0 s +rho Equations = 0.000191 s +U Equations = 0.00134 s +Y Equations = 0.00248712 s +E Equations = 0.000643 s +p Equations = 0.00202 s +calculate parcels = 221.196 s +chemistry correctThermo = 0.002892 s +turbulence correct = 0.001002 s +combustion correct(in Y) = 0.0872169 s +percentage of chemistry = 88.9741 % +percentage of rho/U/Y/E = 4.75503 % +========Time details of each equation======= +rhoEqn Time = 0.000329 s +rhoEqn assamble = 0.000259 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00134 s +UEqn assamble = 0.000821 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000519 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001832 s +YEqn assamble = 0.000644 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000186 s +YEqn correct boundary = 0 s +EEqn Time = 0.000485 s +EEqn assamble = 0.000364 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000121 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 311.45 s ClockTime = 312 s +Courant Number mean: 0.00140751 max: 0.0128567 +Time = 0.002275 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21670 + Current mass in system = 9.82978e-10 + Linear momentum = (1.56719e-11 -4.06311e-09 0) + |Linear momentum| = 4.06314e-09 + Linear kinetic energy = 9.37785e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 462.819, 540.2 + Mass transfer phase change = 7.23165e-10 + D10, D32, Dmax (mu) = 45.566, 67.453, 181.85 + Liquid penetration 95% mass (m) = 0.0140626 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0111674, Final residual = 4.20125e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0823729, Final residual = 1.79243e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.00047304, Final residual = 2.6261e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000219335, Final residual = 1.16176e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000301394, Final residual = 1.79112e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00030145, Final residual = 1.79815e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000404647, Final residual = 1.92427e-08, No Iterations 1 +min/max(T) = 807.123, 2745.07 +GAMG: Solving for p, Initial residual = 0.00809639, Final residual = 5.10167e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.96099e-05, global = 1.91791e-05, cumulative = 0.0165536 +GAMG: Solving for p, Initial residual = 5.08767e-05, Final residual = 5.12379e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.92612e-05, global = 1.92573e-05, cumulative = 0.0165729 +smoothSolver: Solving for epsilon, Initial residual = 0.000554245, Final residual = 5.81895e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000584698, Final residual = 8.07668e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.081778 s +other Time = 0 s +rho Equations = 0.000173 s +U Equations = 0.00149 s +Y Equations = 0.00222412 s +E Equations = 0.000485 s +p Equations = 0.002052 s +calculate parcels = 221.512 s +chemistry correctThermo = 0.001986 s +turbulence correct = 0.000984 s +combustion correct(in Y) = 0.0721909 s +percentage of chemistry = 88.2766 % +percentage of rho/U/Y/E = 5.34633 % +========Time details of each equation======= +rhoEqn Time = 0.000307 s +rhoEqn assamble = 0.000246 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.1e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001489 s +UEqn assamble = 0.000953 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000536 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001532 s +YEqn assamble = 0.000548 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 7.2e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000362 s +EEqn assamble = 0.00027 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.2e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 311.85 s ClockTime = 312 s +Courant Number mean: 0.0014186 max: 0.0128169 +Time = 0.0022775 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21669 + Current mass in system = 9.81304e-10 + Linear momentum = (1.56465e-11 -4.05327e-09 0) + |Linear momentum| = 4.0533e-09 + Linear kinetic energy = 9.34775e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 463.004, 540.2 + Mass transfer phase change = 7.24839e-10 + D10, D32, Dmax (mu) = 45.4996, 67.3908, 181.981 + Liquid penetration 95% mass (m) = 0.01407 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0110682, Final residual = 4.18968e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0840671, Final residual = 1.83515e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000473021, Final residual = 2.60906e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000214834, Final residual = 1.12745e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.00029729, Final residual = 1.75305e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000297344, Final residual = 1.75992e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000405818, Final residual = 1.90295e-08, No Iterations 1 +min/max(T) = 807.117, 2744.97 +GAMG: Solving for p, Initial residual = 0.00863506, Final residual = 5.06545e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.96312e-05, global = 1.92236e-05, cumulative = 0.0165921 +GAMG: Solving for p, Initial residual = 5.05713e-05, Final residual = 5.31608e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.9294e-05, global = 1.92898e-05, cumulative = 0.0166114 +smoothSolver: Solving for epsilon, Initial residual = 0.000546488, Final residual = 5.69873e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000579194, Final residual = 7.95947e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.10373 s +other Time = 0 s +rho Equations = 0.000177 s +U Equations = 0.001227 s +Y Equations = 0.00267649 s +E Equations = 0.000502 s +p Equations = 0.001831 s +calculate parcels = 221.8 s +chemistry correctThermo = 0.002068 s +turbulence correct = 0.00089 s +combustion correct(in Y) = 0.0941655 s +percentage of chemistry = 90.7794 % +percentage of rho/U/Y/E = 4.41771 % +========Time details of each equation======= +rhoEqn Time = 0.000308 s +rhoEqn assamble = 0.000236 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.2e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001227 s +UEqn assamble = 0.000709 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000518 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.00204 s +YEqn assamble = 0.000696 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000352 s +YEqn correct boundary = 0 s +EEqn Time = 0.000385 s +EEqn assamble = 0.000285 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.0001 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 312.24 s ClockTime = 313 s +Courant Number mean: 0.00144624 max: 0.0127843 +Time = 0.00228 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21666 + Current mass in system = 9.79619e-10 + Linear momentum = (1.56133e-11 -4.04328e-09 0) + |Linear momentum| = 4.04331e-09 + Linear kinetic energy = 9.31718e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 463.19, 540.2 + Mass transfer phase change = 7.26524e-10 + D10, D32, Dmax (mu) = 45.443, 67.328, 182.114 + Liquid penetration 95% mass (m) = 0.0140775 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.011655, Final residual = 4.27581e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0852242, Final residual = 1.87279e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000470596, Final residual = 2.57185e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000210171, Final residual = 1.09419e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000292576, Final residual = 1.70894e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000292663, Final residual = 1.71567e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000407549, Final residual = 1.88255e-08, No Iterations 1 +min/max(T) = 807.112, 2744.89 +GAMG: Solving for p, Initial residual = 0.0092607, Final residual = 4.67089e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.97164e-05, global = 1.93502e-05, cumulative = 0.0166307 +GAMG: Solving for p, Initial residual = 4.63669e-05, Final residual = 5.15496e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.94234e-05, global = 1.94204e-05, cumulative = 0.0166501 +smoothSolver: Solving for epsilon, Initial residual = 0.000539217, Final residual = 5.59614e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000573962, Final residual = 7.86742e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.108653 s +other Time = 1e-06 s +rho Equations = 0.000203 s +U Equations = 0.001203 s +Y Equations = 0.00252452 s +E Equations = 0.000602 s +p Equations = 0.002209 s +calculate parcels = 222.138 s +chemistry correctThermo = 0.002872 s +turbulence correct = 0.001123 s +combustion correct(in Y) = 0.0976985 s +percentage of chemistry = 89.9179 % +percentage of rho/U/Y/E = 4.17155 % +========Time details of each equation======= +rhoEqn Time = 0.000357 s +rhoEqn assamble = 0.000282 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001201 s +UEqn assamble = 0.000705 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000496 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001827 s +YEqn assamble = 0.000683 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000169 s +YEqn correct boundary = 0 s +EEqn Time = 0.000443 s +EEqn assamble = 0.00033 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000113 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 312.69 s ClockTime = 313 s +Courant Number mean: 0.00148975 max: 0.0127585 +Time = 0.0022825 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21663 + Current mass in system = 9.77916e-10 + Linear momentum = (1.55682e-11 -4.03309e-09 0) + |Linear momentum| = 4.03312e-09 + Linear kinetic energy = 9.28602e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 463.377, 540.2 + Mass transfer phase change = 7.28227e-10 + D10, D32, Dmax (mu) = 45.3861, 67.2648, 182.247 + Liquid penetration 95% mass (m) = 0.0140862 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0124256, Final residual = 4.29058e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0854928, Final residual = 1.89933e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000463845, Final residual = 2.48343e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000205689, Final residual = 1.06604e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000287535, Final residual = 1.65908e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.00028762, Final residual = 1.6656e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000409141, Final residual = 1.85517e-08, No Iterations 1 +min/max(T) = 807.11, 2744.86 +GAMG: Solving for p, Initial residual = 0.0100101, Final residual = 5.40541e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.99307e-05, global = 1.95475e-05, cumulative = 0.0166697 +GAMG: Solving for p, Initial residual = 5.36716e-05, Final residual = 8.45334e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.96368e-05, global = 1.96317e-05, cumulative = 0.0166893 +smoothSolver: Solving for epsilon, Initial residual = 0.000531613, Final residual = 5.50315e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000568991, Final residual = 7.79672e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.095025 s +other Time = 1e-06 s +rho Equations = 0.000185 s +U Equations = 0.001316 s +Y Equations = 0.00253686 s +E Equations = 0.000598 s +p Equations = 0.002021 s +calculate parcels = 222.487 s +chemistry correctThermo = 0.0029 s +turbulence correct = 0.001001 s +combustion correct(in Y) = 0.0842601 s +percentage of chemistry = 88.6715 % +percentage of rho/U/Y/E = 4.87857 % +========Time details of each equation======= +rhoEqn Time = 0.000328 s +rhoEqn assamble = 0.00026 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001315 s +UEqn assamble = 0.000798 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000517 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001888 s +YEqn assamble = 0.000644 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000231 s +YEqn correct boundary = 0 s +EEqn Time = 0.000442 s +EEqn assamble = 0.000327 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000115 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 313.13 s ClockTime = 314 s +Courant Number mean: 0.00154855 max: 0.0127234 +Time = 0.002285 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21657 + Current mass in system = 9.76198e-10 + Linear momentum = (1.55112e-11 -4.0227e-09 0) + |Linear momentum| = 4.02273e-09 + Linear kinetic energy = 9.25422e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 463.565, 540.2 + Mass transfer phase change = 7.29945e-10 + D10, D32, Dmax (mu) = 45.3776, 67.2013, 182.38 + Liquid penetration 95% mass (m) = 0.0140935 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0136395, Final residual = 4.69834e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0849276, Final residual = 1.91621e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000465873, Final residual = 2.4842e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000201324, Final residual = 1.03992e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000284253, Final residual = 1.62606e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000284335, Final residual = 1.63259e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000412729, Final residual = 1.8424e-08, No Iterations 1 +min/max(T) = 807.111, 2744.83 +GAMG: Solving for p, Initial residual = 0.0108416, Final residual = 6.18255e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.01755e-05, global = 1.97313e-05, cumulative = 0.016709 +GAMG: Solving for p, Initial residual = 6.16078e-05, Final residual = 8.54951e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.98045e-05, global = 1.97988e-05, cumulative = 0.0167288 +smoothSolver: Solving for epsilon, Initial residual = 0.000522192, Final residual = 5.36886e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000562769, Final residual = 7.69093e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.103713 s +other Time = 0 s +rho Equations = 0.000181 s +U Equations = 0.001276 s +Y Equations = 0.00252193 s +E Equations = 0.000633 s +p Equations = 0.002113 s +calculate parcels = 222.837 s +chemistry correctThermo = 0.002886 s +turbulence correct = 0.001022 s +combustion correct(in Y) = 0.0928821 s +percentage of chemistry = 89.5568 % +percentage of rho/U/Y/E = 4.44682 % +========Time details of each equation======= +rhoEqn Time = 0.000331 s +rhoEqn assamble = 0.000263 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001274 s +UEqn assamble = 0.000785 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000489 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001896 s +YEqn assamble = 0.000677 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000208 s +YEqn correct boundary = 0 s +EEqn Time = 0.000472 s +EEqn assamble = 0.000354 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000118 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 313.59 s ClockTime = 314 s +Courant Number mean: 0.00161742 max: 0.0126792 +Time = 0.0022875 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21653 + Current mass in system = 9.74468e-10 + Linear momentum = (1.54398e-11 -4.01209e-09 0) + |Linear momentum| = 4.01212e-09 + Linear kinetic energy = 9.22169e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 463.755, 540.2 + Mass transfer phase change = 7.31675e-10 + D10, D32, Dmax (mu) = 45.3342, 67.1332, 182.513 + Liquid penetration 95% mass (m) = 0.0141022 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0143315, Final residual = 4.7915e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0833611, Final residual = 1.90807e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000463935, Final residual = 2.45438e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000196639, Final residual = 1.01409e-08, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.0002812, Final residual = 1.59226e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000281278, Final residual = 1.59865e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000416597, Final residual = 1.84045e-08, No Iterations 1 +min/max(T) = 807.115, 2744.77 +GAMG: Solving for p, Initial residual = 0.0116806, Final residual = 6.35403e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.03001e-05, global = 1.988e-05, cumulative = 0.0167487 +GAMG: Solving for p, Initial residual = 6.33369e-05, Final residual = 7.45295e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 1.99439e-05, global = 1.99388e-05, cumulative = 0.0167687 +smoothSolver: Solving for epsilon, Initial residual = 0.000512671, Final residual = 5.22413e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000556683, Final residual = 7.586e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.097946 s +other Time = 0 s +rho Equations = 0.000186 s +U Equations = 0.001335 s +Y Equations = 0.00219041 s +E Equations = 0.00049 s +p Equations = 0.001768 s +calculate parcels = 223.179 s +chemistry correctThermo = 0.002049 s +turbulence correct = 0.00081 s +combustion correct(in Y) = 0.0888766 s +percentage of chemistry = 90.7404 % +percentage of rho/U/Y/E = 4.28951 % +========Time details of each equation======= +rhoEqn Time = 0.000323 s +rhoEqn assamble = 0.000254 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.9e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001335 s +UEqn assamble = 0.000798 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000537 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001529 s +YEqn assamble = 0.000565 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000101 s +YEqn correct boundary = 0 s +EEqn Time = 0.000367 s +EEqn assamble = 0.000274 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 314.03 s ClockTime = 315 s +Courant Number mean: 0.00169645 max: 0.0126287 +Time = 0.00229 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21650 + Current mass in system = 9.72717e-10 + Linear momentum = (1.53552e-11 -4.00121e-09 0) + |Linear momentum| = 4.00124e-09 + Linear kinetic energy = 9.18832e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 463.945, 540.2 + Mass transfer phase change = 7.33425e-10 + D10, D32, Dmax (mu) = 45.2664, 67.0619, 182.646 + Liquid penetration 95% mass (m) = 0.0141095 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0142778, Final residual = 4.82539e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0812161, Final residual = 1.88866e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000458699, Final residual = 2.40881e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.00019138, Final residual = 9.89562e-09, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000277252, Final residual = 1.55416e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000277332, Final residual = 1.56054e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000419302, Final residual = 1.8368e-08, No Iterations 1 +min/max(T) = 807.122, 2744.73 +GAMG: Solving for p, Initial residual = 0.0125447, Final residual = 5.74343e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.05085e-05, global = 2.01181e-05, cumulative = 0.0167888 +GAMG: Solving for p, Initial residual = 5.73339e-05, Final residual = 6.00747e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.01812e-05, global = 2.01775e-05, cumulative = 0.016809 +smoothSolver: Solving for epsilon, Initial residual = 0.000503774, Final residual = 5.09148e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000550811, Final residual = 7.49439e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.078873 s +other Time = 0 s +rho Equations = 0.000185 s +U Equations = 0.001186 s +Y Equations = 0.0021703 s +E Equations = 0.000486 s +p Equations = 0.001948 s +calculate parcels = 223.455 s +chemistry correctThermo = 0.001962 s +turbulence correct = 0.000855 s +combustion correct(in Y) = 0.0698237 s +percentage of chemistry = 88.5267 % +percentage of rho/U/Y/E = 5.10606 % +========Time details of each equation======= +rhoEqn Time = 0.000449 s +rhoEqn assamble = 0.000366 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.3e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001185 s +UEqn assamble = 0.00076 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000425 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001601 s +YEqn assamble = 0.000575 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000126 s +YEqn correct boundary = 0 s +EEqn Time = 0.000362 s +EEqn assamble = 0.000269 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.3e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 314.38 s ClockTime = 315 s +Courant Number mean: 0.00178644 max: 0.0125786 +Time = 0.0022925 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21648 + Current mass in system = 9.70945e-10 + Linear momentum = (1.52583e-11 -3.99002e-09 0) + |Linear momentum| = 3.99005e-09 + Linear kinetic energy = 9.15395e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 464.135, 540.2 + Mass transfer phase change = 7.35198e-10 + D10, D32, Dmax (mu) = 45.1863, 66.986, 182.778 + Liquid penetration 95% mass (m) = 0.0141171 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0139781, Final residual = 4.7324e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0787086, Final residual = 1.86418e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000454577, Final residual = 2.33563e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000185956, Final residual = 9.69299e-09, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000273501, Final residual = 1.51944e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000273583, Final residual = 1.52581e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000421416, Final residual = 1.831e-08, No Iterations 1 +min/max(T) = 807.132, 2744.71 +GAMG: Solving for p, Initial residual = 0.0134498, Final residual = 6.00888e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.07675e-05, global = 2.03731e-05, cumulative = 0.0168293 +GAMG: Solving for p, Initial residual = 5.98509e-05, Final residual = 5.80913e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.04319e-05, global = 2.04284e-05, cumulative = 0.0168498 +smoothSolver: Solving for epsilon, Initial residual = 0.000494309, Final residual = 4.95359e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000544908, Final residual = 7.40574e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.118439 s +other Time = 0 s +rho Equations = 0.000266 s +U Equations = 0.00158 s +Y Equations = 0.00303352 s +E Equations = 0.000723 s +p Equations = 0.003062 s +calculate parcels = 223.769 s +chemistry correctThermo = 0.00297 s +turbulence correct = 0.00127 s +combustion correct(in Y) = 0.105254 s +percentage of chemistry = 88.8681 % +percentage of rho/U/Y/E = 4.7303 % +========Time details of each equation======= +rhoEqn Time = 0.000484 s +rhoEqn assamble = 0.000389 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 9.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001578 s +UEqn assamble = 0.000999 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000579 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002302 s +YEqn assamble = 0.00079 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000236 s +YEqn correct boundary = 0 s +EEqn Time = 0.00052 s +EEqn assamble = 0.000394 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000126 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 314.81 s ClockTime = 315 s +Courant Number mean: 0.00188789 max: 0.0125425 +Time = 0.002295 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21643 + Current mass in system = 9.69138e-10 + Linear momentum = (1.51499e-11 -3.97842e-09 0) + |Linear momentum| = 3.97845e-09 + Linear kinetic energy = 9.11831e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 464.326, 540.2 + Mass transfer phase change = 7.37004e-10 + D10, D32, Dmax (mu) = 45.1263, 66.908, 182.91 + Liquid penetration 95% mass (m) = 0.0141245 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0137897, Final residual = 4.73881e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0759664, Final residual = 1.837e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000451627, Final residual = 2.28133e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000180702, Final residual = 9.54677e-09, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000269776, Final residual = 1.49105e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000269856, Final residual = 1.49728e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000423365, Final residual = 1.83204e-08, No Iterations 1 +min/max(T) = 807.145, 2744.68 +GAMG: Solving for p, Initial residual = 0.0143859, Final residual = 5.84618e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.11211e-05, global = 2.07711e-05, cumulative = 0.0168705 +GAMG: Solving for p, Initial residual = 5.87205e-05, Final residual = 6.8712e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.08242e-05, global = 2.08203e-05, cumulative = 0.0168914 +smoothSolver: Solving for epsilon, Initial residual = 0.000483725, Final residual = 4.8163e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000538351, Final residual = 7.32116e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.122343 s +other Time = 0 s +rho Equations = 0.000258 s +U Equations = 0.001508 s +Y Equations = 0.00345056 s +E Equations = 0.000724 s +p Equations = 0.002932 s +calculate parcels = 224.15 s +chemistry correctThermo = 0.002964 s +turbulence correct = 0.001287 s +combustion correct(in Y) = 0.108867 s +percentage of chemistry = 88.9854 % +percentage of rho/U/Y/E = 4.85566 % +========Time details of each equation======= +rhoEqn Time = 0.000473 s +rhoEqn assamble = 0.000385 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 8.8e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001506 s +UEqn assamble = 0.000942 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000564 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.002585 s +YEqn assamble = 0.000943 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 0.000149 s +YEqn correct boundary = 0 s +EEqn Time = 0.000532 s +EEqn assamble = 0.00041 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 0.000122 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 315.32 s ClockTime = 316 s +Courant Number mean: 0.00200141 max: 0.0126099 +Time = 0.0022975 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21632 + Current mass in system = 9.6729e-10 + Linear momentum = (1.50263e-11 -3.96633e-09 0) + |Linear momentum| = 3.96636e-09 + Linear kinetic energy = 9.08115e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 464.518, 540.2 + Mass transfer phase change = 7.38853e-10 + D10, D32, Dmax (mu) = 45.1341, 66.8293, 183.041 + Liquid penetration 95% mass (m) = 0.0141328 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0140833, Final residual = 4.93374e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0730746, Final residual = 1.80504e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000452302, Final residual = 2.32758e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000175614, Final residual = 9.46427e-09, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000265927, Final residual = 1.47659e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000266, Final residual = 1.48273e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.00042632, Final residual = 1.85212e-08, No Iterations 1 +min/max(T) = 807.16, 2744.62 +GAMG: Solving for p, Initial residual = 0.0154127, Final residual = 7.3293e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.16516e-05, global = 2.12615e-05, cumulative = 0.0169126 +GAMG: Solving for p, Initial residual = 7.33573e-05, Final residual = 8.91797e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.13096e-05, global = 2.13047e-05, cumulative = 0.0169339 +smoothSolver: Solving for epsilon, Initial residual = 0.000471386, Final residual = 4.65309e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000530902, Final residual = 7.21171e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.133027 s +other Time = 0 s +rho Equations = 0.000191 s +U Equations = 0.001258 s +Y Equations = 0.0021943 s +E Equations = 0.000477 s +p Equations = 0.001671 s +calculate parcels = 224.508 s +chemistry correctThermo = 0.002036 s +turbulence correct = 0.000831 s +combustion correct(in Y) = 0.12417 s +percentage of chemistry = 93.3417 % +percentage of rho/U/Y/E = 3.09734 % +========Time details of each equation======= +rhoEqn Time = 0.000309 s +rhoEqn assamble = 0.000244 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 6.5e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.001257 s +UEqn assamble = 0.000761 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000496 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001482 s +YEqn assamble = 0.000545 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 5.9e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000359 s +EEqn assamble = 0.000265 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.4e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 315.81 s ClockTime = 316 s +Courant Number mean: 0.0021267 max: 0.0131146 +Time = 0.0023 + + +Solving 2-D cloud sprayCloud +Cloud: sprayCloud + Current number of parcels = 21627 + Current mass in system = 9.65417e-10 + Linear momentum = (1.48908e-11 -3.95377e-09 0) + |Linear momentum| = 3.95379e-09 + Linear kinetic energy = 9.04246e-09 + model1: + number of parcels added = 22711 + mass introduced = 1.70614e-09 + Parcel fate (number, mass) + - escape = 0, 0 + - stick = 0, 0 + Temperature min/max = 464.71, 540.2 + Mass transfer phase change = 7.40726e-10 + D10, D32, Dmax (mu) = 45.0726, 66.7405, 183.171 + Liquid penetration 95% mass (m) = 0.0141402 + +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +smoothSolver: Solving for Ux, Initial residual = 0.0150534, Final residual = 5.29918e-10, No Iterations 2 +smoothSolver: Solving for Uy, Initial residual = 0.0701143, Final residual = 1.76576e-09, No Iterations 2 +=== begin solve_CVODE === +Now DLB algorithm is used!! +=== end solve_CVODE === +DILUPBiCGStab: Solving for C7H16, Initial residual = 0.000451387, Final residual = 2.27966e-08, No Iterations 1 +DILUPBiCGStab: Solving for O2, Initial residual = 0.000171119, Final residual = 9.46417e-09, No Iterations 1 +DILUPBiCGStab: Solving for CO2, Initial residual = 0.000261687, Final residual = 1.45488e-08, No Iterations 1 +DILUPBiCGStab: Solving for H2O, Initial residual = 0.000261754, Final residual = 1.46112e-08, No Iterations 1 +DILUPBiCGStab: Solving for energy, Initial residual = 0.000429453, Final residual = 1.86137e-08, No Iterations 1 +min/max(T) = 807.177, 2744.52 +GAMG: Solving for p, Initial residual = 0.0164504, Final residual = 6.97997e-05, No Iterations 1 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.19619e-05, global = 2.15412e-05, cumulative = 0.0169555 +GAMG: Solving for p, Initial residual = 7.0439e-05, Final residual = 7.14583e-07, No Iterations 2 +diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 +time step continuity errors : sum local = 2.15945e-05, global = 2.159e-05, cumulative = 0.016977 +smoothSolver: Solving for epsilon, Initial residual = 0.000458771, Final residual = 4.51221e-08, No Iterations 1 +smoothSolver: Solving for k, Initial residual = 0.000522993, Final residual = 7.13263e-08, No Iterations 1 +========Time Spent in diffenet parts======== +loop Time = 0.102757 s +other Time = 1e-06 s +rho Equations = 0.000176 s +U Equations = 0.00125 s +Y Equations = 0.00213792 s +E Equations = 0.000496 s +p Equations = 0.001634 s +calculate parcels = 224.845 s +chemistry correctThermo = 0.002037 s +turbulence correct = 0.000818 s +combustion correct(in Y) = 0.0940211 s +percentage of chemistry = 91.4985 % +percentage of rho/U/Y/E = 3.95099 % +========Time details of each equation======= +rhoEqn Time = 0.000304 s +rhoEqn assamble = 0.00023 s +rhoEqn assamble(CPU prepare) = 0 s +rhoEqn assamble(GPU run) = 0 s +rhoEqn solve = 7.4e-05 s +rhoEqn correct boundary = 0 s +UEqn Time = 0.00125 s +UEqn assamble = 0.000718 s +UEqn assamble(CPU prepare) = 0 s +UEqn assamble(GPU run) = 0 s +UEqn solve = 0.000532 s +UEqn correct boundary = 0 s +UEqn H = 0 s +UEqn H(GPU run) = 0 s +UEqn H(correct boundary) = 0 s +UEqn A = 0 s +UEqn A(GPU run) = 0 s +UEqn A(correct boundary) = 0 s +YEqn Time = 0.001437 s +YEqn assamble = 0.000534 s +YEqn assamble(CPU prepare) = 0 s +YEqn assamble(GPU run) = 0 s +YEqn solve = 8.3e-05 s +YEqn correct boundary = 0 s +EEqn Time = 0.000376 s +EEqn assamble = 0.000281 s +EEqn assamble(CPU prepare) = 0 s +EEqn assamble(GPU prepare) = 0 s +EEqn assamble(GPU run) = 0 s +EEqn solve = 9.5e-05 s +EEqn correct boundary = 0 s +pEqn Time = 0 s +pEqn Time solve = 0 s +============================================ + +ExecutionTime = 316.55 s ClockTime = 317 s +End + diff --git a/test/testLoopReport b/test/testLoopReport new file mode 100644 index 00000000..912e0cf1 --- /dev/null +++ b/test/testLoopReport @@ -0,0 +1,4 @@ +Application blockMesh - case .: completed +Application dfLowMachFoam - case .: completed in 316.55 s ClockTime +Application postProcess - case .: completed +