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October 8, 2020, 03:56 |
Help needed in codedSource - mass source
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#1 |
Senior Member
KGN
Join Date: Oct 2009
Location: Chennai, India
Posts: 121
Rep Power: 16 |
I am trying to add mass source using "scalarCodedSource" but the simulation diverges in first iteration itself.
Unit of MFR added here is kg/s Solver i am using is "rhoPimpleFoam" I tried with "scalarSemiImplicitSource" method using hard coded MFR value it works fine. But for my application i have to calculate MFR real time so I am using "codedSource". It can be seen that pressure at the location where "mass Source" is being added goes negative. Please let me know what is wrong with the code.
Code:
massSourceEffusionHole { type scalarCodedSource; name sourceTime0; active true; scalarCodedSourceCoeffs { // Mass source variable fields (rho); selectionMode points; points ( // Sink location i.e. effusion hole inlet (0.035 0.0335 0.0) // Source location i.e. effusion hole exit (0.0385 0.0365 0.0) ); codeInclude #{ #}; codeCorrect #{ #}; codeAddSup #{ Pout<<"Mass Source Start"<<endl; const Time& time = mesh().time(); const volScalarField& rhoJet = mesh_.lookupObject<volScalarField>("rho"); const volVectorField& velJet = mesh_.lookupObject<volVectorField>("U"); const volScalarField& pJet = mesh_.lookupObject<volScalarField>("p"); const scalarField& cellVolume = mesh_.V(); // Adding mass source term scalarField& massSourceEffusionHole = eqn.source(); // Finding the cell corresponding to sink i.e. effusion hole inlet label cellLabelSink = mesh_.findCell(points_[0]); // Finding the cell corresponding to source i.e. effusion hole exit label cellLabelSource = mesh_.findCell(points_[1]); // Calculation of total pressure at Sink scalar totalPJet = pJet[cellLabelSink]+(0.5*rhoJet[cellLabelSink]*pow(mag(velJet[cellLabelSink]),2)); Pout<<"Total Pressure at Sink = "<<totalPJet<<endl; Pout<<"Pressure Source = "<<pJet[cellLabelSource]<<endl; // Calculation of MFR at Sink scalar mfrSink = totalPJet*pow((pJet[cellLabelSource]/totalPJet),0.8571)*1.3212*1e-6*sqrt(((2.0*1.4)/(0.4*287.05*300))*(pow((totalPJet/pJet[cellLabelSource]),0.2857)-1)); Pout<<"MFR Sink = "<<mfrSink<<endl; massSourceEffusionHole[cellLabelSource] += mfrSink; Pout<<"MFR Sink = "<<massSourceEffusionHole[cellLabelSource]<<endl; Pout<<"Mass Source End"<<endl; #}; codeSetValue #{ #} // Dummy entry. Make dependent on above to trigger recompilation code #{ $codeInclude $codeCorrect $codeAddSup $codeSetValue #}; } sourceTime0Coeffs { $scalarCodedSourceCoeffs; } } Code:
Time = 1 Using dynamicCode for fvOption:: sourceTime0 at line 72 in "/home/system/Projects/Siragugal/GasTubineCombustor/EffusionHoleModel/singleHoleFlatPlate_EffusionBC/constant/fvOptions.massSourceEffusionHole.scalarCodedSourceCoeffs" Selecting finite volume options model type sourceTime0 Source: sourceTime0 - selecting cells using points - selected 2 cell(s) with volume 2.3806788e-10 Mass Source Start Total Pressure at Sink = 220796.55 Pressure Source = 200000 MFR Sink = 0.00040910048 MFR Sink = 0.00040910048 Mass Source End diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 smoothSolver: Solving for Ux, Initial residual = 0.0032980687, Final residual = 8.0245382e-07, No Iterations 16 smoothSolver: Solving for Uy, Initial residual = 0.99999999, Final residual = 8.8311766e-07, No Iterations 23 smoothSolver: Solving for Uz, Initial residual = 0.99999999, Final residual = 6.778778e-07, No Iterations 15 smoothSolver: Solving for e, Initial residual = 4.2580813e-05, Final residual = 3.1907154e-07, No Iterations 1 Mass Source Start Total Pressure at Sink = 220796.55 Pressure Source = 200000 MFR Sink = 0.00040910048 MFR Sink = 0.00040910048 Mass Source End GAMG: Solving for p, Initial residual = 0.00022212445, Final residual = 1.8957863e-05, No Iterations 17 GAMG: Solving for p, Initial residual = 0.00029171794, Final residual = 2.5683858e-05, No Iterations 2 Mass Source Start Total Pressure at Sink = 220796.54 Pressure Source = 61287.67 MFR Sink = 0.0005830456 MFR Sink = 0.0005830456 Mass Source End diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.0513006e-05, global = -7.3666193e-06, cumulative = -7.3666193e-06 Mass Source Start Total Pressure at Sink = 220796.56 Pressure Source = 61287.67 MFR Sink = 0.00058304562 MFR Sink = 0.00058304562 Mass Source End GAMG: Solving for p, Initial residual = 0.00027760611, Final residual = 2.3000663e-05, No Iterations 11 GAMG: Solving for p, Initial residual = 0.00017927573, Final residual = 9.6137966e-07, No Iterations 31 Mass Source Start Total Pressure at Sink = 220796.57 Pressure Source = -50175.002 #0 Foam::error::printStack(Foam::Ostream&) at ??:? #1 Foam::sigFpe::sigHandler(int) at ??:? #2 ? in "/lib/x86_64-linux-gnu/libc.so.6" #3 ? in "/lib/x86_64-linux-gnu/libm.so.6" #4 pow in "/lib/x86_64-linux-gnu/libm.so.6" #5 Foam::fv::sourceTime0FvOptionscalarSource::addSup(Foam::fvMatrix<double>&, int) at constant/fvOptions.massSourceEffusionHole.scalarCodedSourceCoeffs:114 #6 ? in "/home/system/OpenFOAM/OpenFOAM-6/platforms/linux64GccDPInt32Opt/bin/rhoPimpleFoam" #7 ? in "/home/system/OpenFOAM/OpenFOAM-6/platforms/linux64GccDPInt32Opt/bin/rhoPimpleFoam" #8 ? in "/home/system/OpenFOAM/OpenFOAM-6/platforms/linux64GccDPInt32Opt/bin/rhoPimpleFoam" #9 __libc_start_main in "/lib/x86_64-linux-gnu/libc.so.6" #10 ? in "/home/system/OpenFOAM/OpenFOAM-6/platforms/linux64GccDPInt32Opt/bin/rhoPimpleFoam" Floating point exception (core dumped) |
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October 12, 2020, 04:07 |
Please help with "codedSource"
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#2 |
Senior Member
KGN
Join Date: Oct 2009
Location: Chennai, India
Posts: 121
Rep Power: 16 |
Still I am having the same problem.
Is there any specific code to be added for "rhoPimpleFoam" solver? Simulation diverging in first iteration itself.. bcz of pressure going negative at the cell where mass source is being added.. |
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