/*---------------------------------------------------------------------------*\ | ========= | | | \\ / F ield | OpenFOAM: The Open Source CFD Toolbox | | \\ / O peration | Version: 2.1.x | | \\ / A nd | Web: www.OpenFOAM.org | | \\/ M anipulation | | \*---------------------------------------------------------------------------*/ Build : 2.1.x-2bd9ad2cb028 Exec : LTSReactingParcelFoam Date : Mar 04 2013 Time : 18:15:18 Host : "kalle-desktop" PID : 12629 Case : /home/kalle/OpenFOAM/kalle-2.1.x/run/verticalChannel nProcs : 1 sigFpe : Enabling floating point exception trapping (FOAM_SIGFPE). fileModificationChecking : Monitoring run-time modified files using timeStampMaster allowSystemOperations : Disallowing user-supplied system call operations // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // Create time Create mesh for time = 0 Reading g PIMPLE: Operating solver in PISO mode Creating combustion model Selecting combustion model PaSR Selecting rhoChemistryModel ODEChemistryModel Selecting thermodynamics package hsRhoMixtureThermo> Selecting chemistryReader foamChemistryReader ODEChemistryModel: Number of species = 2 and reactions = 0 Creating component thermo properties: multi-component carrier - 2 species liquids - 1 components solids - 0 components Reading field U Reading/calculating face flux field phi Creating turbulence model Selecting turbulence model type RASModel Selecting RAS turbulence model kOmegaSST kOmegaSSTCoeffs { alphaK1 0.85034; alphaK2 1; alphaOmega1 0.5; alphaOmega2 0.85616; Prt 1; gamma1 0.5532; gamma2 0.4403; beta1 0.075; beta2 0.0828; betaStar 0.09; a1 0.31; b1 1; c1 10; F3 false; } Creating multi-variate interpolation scheme Selecting radiationModel none Constructing reacting cloud Constructing particle forces Selecting particle force sphereDrag Selecting particle force gravity Constructing cloud functions Selecting cloud function patchPostProcessing --> FOAM Warning : From function Foam::PatchPostProcessing::PatchPostProcessing(const dictionary&, CloudType& ) in file lnInclude/PatchPostProcessing.C at line 170 Cannot find any patch names matching out Selecting cloud function particleTracks Selecting dispersion model stochasticDispersionRAS Selecting injection model coneNozzleInjection Constructing 3-D injection Selecting distribution model general Selecting patch interaction model standardWallInteraction Selecting surface film model none Selecting U integration scheme Euler Selecting heat transfer model RanzMarshall Selecting T integration scheme analytical Selecting composition model singleMixtureFraction --> FOAM Warning : From function phaseProperties::initialiseGlobalIds(...) in file phaseProperties/phaseProperties/phaseProperties.C at line 231 Assuming no mapping between solid and carrier species Selecting phase change model liquidEvaporation Participating liquid species: H2O Selecting devolatilisation model none Selecting surface reaction model none Creating sources Creating field source list from sourcesProperties Creating porous zones Starting time loop faceSource faceSource1: total faces = 300 total area = 0.00125 weight field = phi Time = 1 Time scales min/max: Flow = 0.0004194877178, 1 Temperature = 0.5239990615, 1 Overall = 0.0004194877178, 1 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.6033086007, 2.517408764 smoothSolver: Solving for omega, Initial residual = 0.04750035747, Final residual = 0.004309339736, No Iterations 5 smoothSolver: Solving for k, Initial residual = 1, Final residual = 0.005935611755, No Iterations 1 smoothSolver: Solving for Ux, Initial residual = 1, Final residual = 0.09764040962, No Iterations 1 smoothSolver: Solving for Uy, Initial residual = 1, Final residual = 0.06466864044, No Iterations 2 smoothSolver: Solving for Uz, Initial residual = 1, Final residual = 0.02456368978, No Iterations 2 smoothSolver: Solving for H2O, Initial residual = 0.000484509329, Final residual = 0.0003834732576, No Iterations 20 smoothSolver: Solving for hs, Initial residual = 1, Final residual = 0.0241806176, No Iterations 2 T gas min/max = 473, 573 GAMG: Solving for p, Initial residual = 0.9999999762, Final residual = 0.03847485715, No Iterations 12 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = -0.6324729952, 11.13444544 time step continuity errors : sum local = 0.3842843677, global = 0.08406852739, cumulative = 0.08406852739 p min/max = 100000, 101816.588 GAMG: Solving for p, Initial residual = 0.003421156494, Final residual = 0.0001531153557, No Iterations 10 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = -15.67957583, 2.975493597 time step continuity errors : sum local = 0.7702027734, global = -0.1757867934, cumulative = -0.09171826601 p min/max = 100000, 100264.0484 ExecutionTime = 1.56 s ClockTime = 2 s Time = 2 Time scales min/max: Flow = 0.0002061791731, 0.003449812096 Temperature = 1, 1 Overall = 0.0002061791731, 0.002901935068 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.5892116672, 0.7233091713 smoothSolver: Solving for omega, Initial residual = 0.1016267889, Final residual = 0.003659048008, No Iterations 1 smoothSolver: Solving for k, Initial residual = 0.3120208201, Final residual = 0.006930748697, No Iterations 2 smoothSolver: Solving for Ux, Initial residual = 0.4038783394, Final residual = 0.03902398294, No Iterations 1 smoothSolver: Solving for Uy, Initial residual = 0.03644645491, Final residual = 0.00136082744, No Iterations 2 smoothSolver: Solving for Uz, Initial residual = 0.1898211059, Final residual = 0.009511055972, No Iterations 1 smoothSolver: Solving for H2O, Initial residual = 0.0006709729124, Final residual = 0.0002303606973, No Iterations 20 smoothSolver: Solving for hs, Initial residual = 0.2607967564, Final residual = 0.01102568197, No Iterations 3 T gas min/max = 472.9899485, 573 GAMG: Solving for p, Initial residual = 0.2998056926, Final residual = 0.01092200902, No Iterations 5 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.6033086007, 0.7352453458 time step continuity errors : sum local = 0.0002930972349, global = 6.421606496e-05, cumulative = -0.09165404994 p min/max = 100000, 103457.383 GAMG: Solving for p, Initial residual = 0.02277783075, Final residual = 0.001131781789, No Iterations 6 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.6033086007, 0.7389276892 time step continuity errors : sum local = 0.0002935090766, global = 0.0002431148904, cumulative = -0.09141093505 p min/max = 100000, 101453.3994 ExecutionTime = 2.25 s ClockTime = 2 s Time = 3 Time scales min/max: Flow = 0.0002439985567, 0.003169159402 Temperature = 1, 1 Overall = 0.0002439985567, 0.002888289355 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.5646745442, 0.7387274656 smoothSolver: Solving for omega, Initial residual = 0.04819780151, Final residual = 0.001868125665, No Iterations 1 smoothSolver: Solving for k, Initial residual = 0.1640653524, Final residual = 0.007374866803, No Iterations 2 smoothSolver: Solving for Ux, Initial residual = 0.239683454, Final residual = 0.005282198834, No Iterations 2 smoothSolver: Solving for Uy, Initial residual = 0.1174428247, Final residual = 0.007351000883, No Iterations 1 smoothSolver: Solving for Uz, Initial residual = 0.5780677619, Final residual = 0.03101146595, No Iterations 1 smoothSolver: Solving for H2O, Initial residual = 0.0003527258206, Final residual = 0.0002313263155, No Iterations 20 smoothSolver: Solving for hs, Initial residual = 0.1622548544, Final residual = 0.009870124196, No Iterations 3 T gas min/max = 472.9815876, 573 GAMG: Solving for p, Initial residual = 0.03362969083, Final residual = 0.001471870253, No Iterations 7 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.6033086007, 0.7205328726 time step continuity errors : sum local = 0.0001705301086, global = -3.449156757e-05, cumulative = -0.09144542662 p min/max = 97197.46494, 100000.4875 GAMG: Solving for p, Initial residual = 0.009993951108, Final residual = 0.0003634235381, No Iterations 8 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.6033086007, 0.7193872505 time step continuity errors : sum local = 8.45808328e-05, global = -6.809480022e-05, cumulative = -0.09151352142 p min/max = 99969.34472, 100095.1368 ExecutionTime = 3.01 s ClockTime = 3 s Time = 4 Time scales min/max: Flow = 0.0002544996389, 0.003245709978 Temperature = 1, 1 Overall = 0.0002544996389, 0.002908792238 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.5929170624, 0.7193884821 smoothSolver: Solving for omega, Initial residual = 0.02634397323, Final residual = 0.001287381972, No Iterations 1 smoothSolver: Solving for k, Initial residual = 0.09850575454, Final residual = 0.007047670194, No Iterations 2 smoothSolver: Solving for Ux, Initial residual = 0.1690762141, Final residual = 0.003828601592, No Iterations 2 smoothSolver: Solving for Uy, Initial residual = 0.02317255761, Final residual = 0.002146757604, No Iterations 1 smoothSolver: Solving for Uz, Initial residual = 0.5271099166, Final residual = 0.03286312378, No Iterations 1 smoothSolver: Solving for H2O, Initial residual = 0.0003259149725, Final residual = 0.0002318611203, No Iterations 20 smoothSolver: Solving for hs, Initial residual = 0.10036586, Final residual = 0.006941720595, No Iterations 3 T gas min/max = 472.978946, 573 GAMG: Solving for p, Initial residual = 0.2726576953, Final residual = 0.01273985367, No Iterations 5 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.6033086007, 0.7245454381 time step continuity errors : sum local = 8.52764475e-05, global = 2.119853497e-05, cumulative = -0.09149232288 p min/max = 99983.53538, 100072.4887 GAMG: Solving for p, Initial residual = 0.08844705856, Final residual = 0.003265794315, No Iterations 4 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.6033086007, 0.7217790114 time step continuity errors : sum local = 3.553513718e-05, global = 1.911174547e-05, cumulative = -0.09147321114 p min/max = 99999.89337, 100088.6935 ExecutionTime = 3.65 s ClockTime = 4 s Time = 5 Solving cloud reactingCloud1 --> Cloud: reactingCloud1 Added 53 new parcels Cloud: reactingCloud1 Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 Total number of parcels added = 53 Total mass introduced = 0.000424 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 1e+15, 0 Mass transfer phase change = 0.000424 Mass transfer devolatilisation = 0 Mass transfer surface reaction = 0 Time scales min/max: Flow = 0.0002541651657, 0.003508028292 Temperature = 0.003207719715, 1 Overall = 0.0002541651657, 0.002973222898 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = -0.8917089957, 0.7218354862 smoothSolver: Solving for omega, Initial residual = 0.01696838243, Final residual = 0.0009192595052, No Iterations 1 smoothSolver: Solving for k, Initial residual = 0.06795125874, Final residual = 0.005928654665, No Iterations 2 smoothSolver: Solving for Ux, Initial residual = 0.1284137804, Final residual = 0.01198509792, No Iterations 1 smoothSolver: Solving for Uy, Initial residual = 0.02214253426, Final residual = 0.001845329931, No Iterations 1 smoothSolver: Solving for Uz, Initial residual = 0.2944703306, Final residual = 0.02605353451, No Iterations 1 smoothSolver: Solving for H2O, Initial residual = 0.9999999985, Final residual = 0.05389570425, No Iterations 1 smoothSolver: Solving for hs, Initial residual = 0.07396607239, Final residual = 0.004910960219, No Iterations 3 T gas min/max = 427.2453241, 573 GAMG: Solving for p, Initial residual = 0.0801234021, Final residual = 0.003445397845, No Iterations 5 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.420804354, 0.7227392346 time step continuity errors : sum local = 4.505456729e-05, global = -1.21683128e-05, cumulative = -0.09148537945 p min/max = 100000, 100192.5926 GAMG: Solving for p, Initial residual = 0.04832210249, Final residual = 0.002185182621, No Iterations 5 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.4207867875, 0.7227478005 time step continuity errors : sum local = 2.533041163e-05, global = 1.683088129e-05, cumulative = -0.09146854857 p min/max = 100000, 100137.6067 ExecutionTime = 5.08 s ClockTime = 5 s Time = 6 Time scales min/max: Flow = 0.0002530365824, 0.003639094927 Temperature = 0.003793198311, 1 Overall = 0.0002530365824, 0.003019129411 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.2956983493, 0.7262480787 smoothSolver: Solving for omega, Initial residual = 0.01249299269, Final residual = 0.0006866295687, No Iterations 1 smoothSolver: Solving for k, Initial residual = 0.05157899977, Final residual = 0.004637621629, No Iterations 2 smoothSolver: Solving for Ux, Initial residual = 0.107291549, Final residual = 0.009726178501, No Iterations 1 smoothSolver: Solving for Uy, Initial residual = 0.0200363767, Final residual = 0.001570947917, No Iterations 1 smoothSolver: Solving for Uz, Initial residual = 0.2976224513, Final residual = 0.02148078468, No Iterations 1 smoothSolver: Solving for H2O, Initial residual = 0.3410435983, Final residual = 0.008563331649, No Iterations 1 smoothSolver: Solving for hs, Initial residual = 0.06044468981, Final residual = 0.003482850105, No Iterations 3 T gas min/max = 371.2612889, 573 GAMG: Solving for p, Initial residual = 0.07695364616, Final residual = 0.002919599437, No Iterations 5 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.5248735705, 0.7260061084 time step continuity errors : sum local = 3.133095919e-05, global = -7.000048311e-06, cumulative = -0.09147554862 p min/max = 99936.1633, 100013.8607 GAMG: Solving for p, Initial residual = 0.1103991662, Final residual = 0.004909507154, No Iterations 5 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.524850714, 0.7259968079 time step continuity errors : sum local = 2.202072805e-05, global = 7.811578824e-06, cumulative = -0.09146773704 p min/max = 99968.65632, 100062.7226 ExecutionTime = 5.71 s ClockTime = 6 s Time = 7 Time scales min/max: Flow = 0.0002533450094, 0.003908936908 Temperature = 0.003689437757, 1 Overall = 0.0002533450094, 0.003074003568 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.3478968606, 0.7292960416 smoothSolver: Solving for omega, Initial residual = 0.01040341452, Final residual = 0.0005536751392, No Iterations 1 smoothSolver: Solving for k, Initial residual = 0.04144327362, Final residual = 0.003571856688, No Iterations 2 smoothSolver: Solving for Ux, Initial residual = 0.09365403597, Final residual = 0.008002511997, No Iterations 1 smoothSolver: Solving for Uy, Initial residual = 0.01842257438, Final residual = 0.001436555504, No Iterations 1 smoothSolver: Solving for Uz, Initial residual = 0.2837828403, Final residual = 0.02069967424, No Iterations 1 smoothSolver: Solving for H2O, Initial residual = 0.07744854302, Final residual = 0.001169918475, No Iterations 1 smoothSolver: Solving for hs, Initial residual = 0.04865945547, Final residual = 0.002528356238, No Iterations 3 T gas min/max = 338.7127412, 573 GAMG: Solving for p, Initial residual = 0.121213296, Final residual = 0.004036023307, No Iterations 4 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.550931736, 0.7290271926 time step continuity errors : sum local = 2.217829361e-05, global = 4.817023758e-06, cumulative = -0.09146292002 p min/max = 100000, 100211.0622 GAMG: Solving for p, Initial residual = 0.02066572989, Final residual = 0.0009608057085, No Iterations 3 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.550931736, 0.7290257698 time step continuity errors : sum local = 1.457868841e-05, global = -7.469651032e-06, cumulative = -0.09147038967 p min/max = 100000, 100139.7025 ExecutionTime = 6.29 s ClockTime = 7 s Time = 8 Time scales min/max: Flow = 0.0002512366408, 0.005019691212 Temperature = 0.003690604376, 1 Overall = 0.0002512366408, 0.003125122734 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.5351583377, 0.7321108418 smoothSolver: Solving for omega, Initial residual = 0.008762087074, Final residual = 0.0004609335181, No Iterations 1 smoothSolver: Solving for k, Initial residual = 0.03455509286, Final residual = 0.002734747298, No Iterations 2 smoothSolver: Solving for Ux, Initial residual = 0.0829282036, Final residual = 0.006850943704, No Iterations 1 smoothSolver: Solving for Uy, Initial residual = 0.01940771642, Final residual = 0.001485079971, No Iterations 1 smoothSolver: Solving for Uz, Initial residual = 0.1435163483, Final residual = 0.0105534477, No Iterations 1 smoothSolver: Solving for H2O, Initial residual = 0.04743256047, Final residual = 0.0009159652013, No Iterations 1 smoothSolver: Solving for hs, Initial residual = 0.04165617526, Final residual = 0.001857046418, No Iterations 3 T gas min/max = 317.0883551, 573 GAMG: Solving for p, Initial residual = 0.04584983822, Final residual = 0.001553785295, No Iterations 4 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.5942802454, 0.7458511237 time step continuity errors : sum local = 1.98008752e-05, global = -5.51650634e-06, cumulative = -0.09147590617 p min/max = 99945.66362, 100028.9862 GAMG: Solving for p, Initial residual = 0.05609143556, Final residual = 0.001906502671, No Iterations 5 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.594287949, 0.7458561414 time step continuity errors : sum local = 1.110854048e-05, global = 2.238787189e-06, cumulative = -0.09147366739 p min/max = 99982.58991, 100090.644 ExecutionTime = 6.9 s ClockTime = 7 s Time = 9 Time scales min/max: Flow = 0.0002498059014, 0.006395871948 Temperature = 0.003736827711, 1 Overall = 0.0002498059014, 0.003184530249 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.5942902654, 0.7762922393 smoothSolver: Solving for omega, Initial residual = 0.008181464086, Final residual = 0.0004047393322, No Iterations 1 smoothSolver: Solving for k, Initial residual = 0.02958636552, Final residual = 0.002091047911, No Iterations 2 smoothSolver: Solving for Ux, Initial residual = 0.07674907159, Final residual = 0.006042428145, No Iterations 1 smoothSolver: Solving for Uy, Initial residual = 0.01724885056, Final residual = 0.001341972799, No Iterations 1 smoothSolver: Solving for Uz, Initial residual = 0.1130306904, Final residual = 0.008844947275, No Iterations 1 smoothSolver: Solving for H2O, Initial residual = 0.033520871, Final residual = 0.0005613631644, No Iterations 1 smoothSolver: Solving for hs, Initial residual = 0.03640096058, Final residual = 0.003400121071, No Iterations 2 T gas min/max = 302.6082573, 573 GAMG: Solving for p, Initial residual = 0.0787364791, Final residual = 0.00349682018, No Iterations 4 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.6033086007, 0.7753574059 time step continuity errors : sum local = 2.05523651e-05, global = 5.835845739e-06, cumulative = -0.09146783154 p min/max = 99823.47682, 100000 GAMG: Solving for p, Initial residual = 0.02542738776, Final residual = 0.0009118951131, No Iterations 6 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 rho min/max = 0.6033086007, 0.7753662246 time step continuity errors : sum local = 1.280416986e-05, global = 2.262484498e-06, cumulative = -0.09146556906 p min/max = 99949.95017, 100009.0098 ExecutionTime = 7.53 s ClockTime = 8 s Time = 10 Solving cloud reactingCloud1 --> FOAM FATAL ERROR: object is not allocated From function Foam::autoPtr::operator->() in file /home/kalle/OpenFOAM/OpenFOAM-2.1.x/src/OpenFOAM/lnInclude/autoPtrI.H at line 153. FOAM aborting #0 Foam::error::printStack(Foam::Ostream&) in "/home/kalle/OpenFOAM/OpenFOAM-2.1.x/platforms/linux64GccDPOpt/lib/libOpenFOAM.so" #1 Foam::error::abort() in "/home/kalle/OpenFOAM/OpenFOAM-2.1.x/platforms/linux64GccDPOpt/lib/libOpenFOAM.so" #2 Foam::ConeNozzleInjection > > > > > >::setProperties(int, int, double, Foam::ReactingMultiphaseParcel > > >&) in "/home/kalle/OpenFOAM/OpenFOAM-2.1.x/platforms/linux64GccDPOpt/lib/liblagrangianIntermediate.so" #3 in "/home/kalle/OpenFOAM/OpenFOAM-2.1.x/platforms/linux64GccDPOpt/bin/LTSReactingParcelFoam" #4 in "/home/kalle/OpenFOAM/OpenFOAM-2.1.x/platforms/linux64GccDPOpt/bin/LTSReactingParcelFoam" #5 in "/home/kalle/OpenFOAM/OpenFOAM-2.1.x/platforms/linux64GccDPOpt/bin/LTSReactingParcelFoam" #6 in "/home/kalle/OpenFOAM/OpenFOAM-2.1.x/platforms/linux64GccDPOpt/bin/LTSReactingParcelFoam" #7 __libc_start_main in "/lib/x86_64-linux-gnu/libc.so.6" #8 in "/home/kalle/OpenFOAM/OpenFOAM-2.1.x/platforms/linux64GccDPOpt/bin/LTSReactingParcelFoam" Aborted (core dumped)