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July 13, 2009, 09:52 |
Problems with simulating TurbFOAM
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#1 |
New Member
Barath Ezhilan
Join Date: Jun 2009
Posts: 20
Rep Power: 16 |
Hi All,
I am trying to simulate swirling flow in the draft tube of the turbine using KOmegaSST turbulence model with TurbFOAM and I am having a problem with it. The simulations stops after a few time steps. I have a delta T 1e-5 and I have also tried increasing the number of correctors and orthogonal correctors etc. The Mesh is fine, checkMesh says the Mesh is OK. I have also checked the boundary files The log file::: Time = 9.55556e-05 Courant Number mean: 0.00131032 max: 7.52485 velocity magnitude: 260.087 PBiCG: Solving for Ux, Initial residual = 0.104884, Final residual = 0.00497614, No Iterations 2 PBiCG: Solving for Uy, Initial residual = 0.110647, Final residual = 0.00209042, No Iterations 2 PBiCG: Solving for Uz, Initial residual = 0.0109506, Final residual = 0.000402031, No Iterations 2 PCG: Solving for p, Initial residual = 0.905193, Final residual = 0.00849971, No Iterations 19 time step continuity errors : sum local = 3.95906e-06, global = 2.96857e-08, cumulative = 2.60243e-07 PCG: Solving for p, Initial residual = 0.903698, Final residual = 0.0077981, No Iterations 21 time step continuity errors : sum local = 5.59011e-06, global = 2.96251e-08, cumulative = 2.89868e-07 PBiCG: Solving for omega, Initial residual = 0.0521617, Final residual = 0.00171759, No Iterations 2 bounding omega, min: -3.10703e+06 max: 1.37457e+07 average: 6537.53 PBiCG: Solving for k, Initial residual = 0.0759318, Final residual = 0.00116278, No Iterations 2 bounding k, min: -0.228331 max: 4.29478 average: 0.0111114 ExecutionTime = 293.4 s ClockTime = 295 s Time = 0.000105556 Courant Number mean: 0.00177524 max: 16.8808 velocity magnitude: 532.235 PBiCG: Solving for Ux, Initial residual = 0.207847, Final residual = 0.0171767, No Iterations 2 PBiCG: Solving for Uy, Initial residual = 0.230103, Final residual = 0.0131825, No Iterations 2 PBiCG: Solving for Uz, Initial residual = 0.0368306, Final residual = 0.00168079, No Iterations 2 PCG: Solving for p, Initial residual = 0.905287, Final residual = 0.00834842, No Iterations 24 time step continuity errors : sum local = 7.86545e-06, global = 3.42434e-08, cumulative = 3.24111e-07 PCG: Solving for p, Initial residual = 0.909423, Final residual = 0.00750422, No Iterations 24 time step continuity errors : sum local = 1.0548e-05, global = 3.40615e-08, cumulative = 3.58173e-07 PBiCG: Solving for omega, Initial residual = 0.0586053, Final residual = 0.00481685, No Iterations 2 bounding omega, min: -1.3806e+07 max: 2.58179e+07 average: 13489.3 PBiCG: Solving for k, Initial residual = 0.0920886, Final residual = 0.00343743, No Iterations 2 bounding k, min: -1.52212 max: 6.6377 average: 0.0125395 ExecutionTime = 307.73 s ClockTime = 309 s Time = 0.000115556 Courant Number mean: 0.00234709 max: 21.606 velocity magnitude: 748.857 PBiCG: Solving for Ux, Initial residual = 0.344634, Final residual = 0.0099675, No Iterations 3 PBiCG: Solving for Uy, Initial residual = 0.329588, Final residual = 0.0101443, No Iterations 3 PBiCG: Solving for Uz, Initial residual = 0.0829345, Final residual = 0.00185229, No Iterations 3 PCG: Solving for p, Initial residual = 0.894228, Final residual = 0.0069595, No Iterations 77 time step continuity errors : sum local = 1.32459e-05, global = 3.74457e-08, cumulative = 3.95619e-07 PCG: Solving for p, Initial residual = 0.941143, Final residual = 0.00818695, No Iterations 100 time step continuity errors : sum local = 4.97055e-05, global = 3.5411e-08, cumulative = 4.3103e-07 PBiCG: Solving for omega, Initial residual = 1, Final residual = 0.0738547, No Iterations 76 bounding omega, min: -1.39421e+19 max: 2.83497e+19 average: 8.33634e+14 PBiCG: Solving for k, Initial residual = 0.929398, Final residual = 2.79674e-11, No Iterations 1 bounding k, min: -1.05884 max: 9.29845 average: 0.00995458 ExecutionTime = 347.03 s ClockTime = 349 s Time = 0.000125556 Courant Number mean: 0.0842083 max: 107356 velocity magnitude: 6.87564e+06 PBiCG: Solving for Ux, Initial residual = 0.999926, Final residual = 5.05889, No Iterations 1000 PBiCG: Solving for Uy, Initial residual = 0.999817, Final residual = 15.8907, No Iterations 1000 PBiCG: Solving for Uz, Initial residual = 0.999843, Final residual = 6.45841, No Iterations 1000 PCG: Solving for p, Initial residual = 0.999999, Final residual = 0.415433, No Iterations 1000 time step continuity errors : sum local = 6410.55, global = 3.66894e-08, cumulative = 4.67719e-07 PCG: Solving for p, Initial residual = 0.996811, Final residual = 0.317644, No Iterations 1000 time step continuity errors : sum local = 1.70248e+06, global = 3.65351e-08, cumulative = 5.04254e-07 ~ The files in the system folder are given below ControlDict:::: application turbFoam; startFrom latestTime; startTime 0; stopAt endTime; endTime 0.3; deltaT 0.00005; writeControl timeStep; writeInterval 50; purgeWrite 0; writeFormat ascii; writePrecision 6; writeCompression compressed; timeFormat general; timePrecision 6; runTimeModifiable no; // libs ("libaddedIncompressibleRASModels.so"); libs ("libOpenFoamTurbo.so" ); Schemes File:: ddtSchemes { default Euler; } gradSchemes { default Gauss linear; grad(p) Gauss linear; grad(U) Gauss linear; } divSchemes { default none; div(phi,U) Gauss limitedLinearV 1; div(phi,k) Gauss limitedLinear 1; div(phi,epsilon) Gauss limitedLinear 1; div(phi,omega) Gauss limitedLinear 1; div(phi,R) Gauss limitedLinear 1; div(R) Gauss linear; div(phi,nuTilda) Gauss limitedLinear 1; div((nuEff*dev(grad(U).T()))) Gauss linear; } laplacianSchemes { default none; laplacian(nuEff,U) Gauss linear corrected; laplacian((1|A(U)),p) Gauss linear corrected; laplacian(DkEff,k) Gauss linear corrected; laplacian(DepsilonEff,epsilon) Gauss linear corrected; laplacian(DomegaEff,omega) Gauss linear corrected; laplacian(DREff,R) Gauss linear corrected; laplacian(DnuTildaEff,nuTilda) Gauss linear corrected; } interpolationSchemes { default linear; interpolate(U) linear; } snGradSchemes { default corrected; } fluxRequired { default no; p; } Solution File:: solvers { p PCG { preconditioner DIC; tolerance 1e-06; relTol 0.01; }; U PBiCG { preconditioner DILU; tolerance 1e-05; relTol 0.1; }; k PBiCG { preconditioner DILU; tolerance 1e-05; relTol 0.1; }; epsilon PBiCG { preconditioner DILU; tolerance 1e-05; relTol 0.1; }; omega PBiCG { preconditioner DILU; tolerance 1e-05; relTol 0.1; }; R PBiCG { preconditioner DILU; tolerance 1e-05; relTol 0.1; }; nuTilda PBiCG { preconditioner DILU; tolerance 1e-05; relTol 0.1; }; PISO { nCorrectors 4; nNonOrthogonalCorrectors 2; pRefCell 0; pRefValue 0; } Please do help me this regard as to what I can do to solve this problem??? |
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Tags |
courant number increasing, turbfoam |
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