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March 8, 2011, 06:58 |
pisoFsiFoam
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#1 |
New Member
Charbel Habchi
Join Date: Jan 2011
Location: Lebanon
Posts: 27
Rep Power: 15 |
Hi,
I make pisoFsiFoam to solve fluid structure interaction in turbulent flow basing on icoFsiFoam. In fact I only modified the fluid solver. The pisoFsiFoam and a 2D test case can be obtained from the following link: http://dl.free.fr/azoxbwmku After compiling this solver I tried it for the simple 2D case. But the solver stops after the first time step without showing error message. In fact the message I have from the log.pisoFsiFoam file is below: // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // Build : 1.6-ext Exec : pisoFsiFoam Case : /home/charbel.habchi/OpenFOAM/charbel.habchi-1.6-ext/run/vorflex/pisoFsiFoam2DTestCase/fluid nProcs : 1 SigFpe : Enabling floating point exception trapping (FOAM_SIGFPE). // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // Create time Create dynamic mesh for time = 0 Selecting dynamicFvMesh dynamicMotionSolverFvMesh // using new solver syntax: p { solver PCG; preconditioner DIC; tolerance 1e-06; relTol 0; } // using new solver syntax: U { solver PBiCG; preconditioner DILU; tolerance 1e-05; relTol 0; } Selecting motion solver: laplaceFaceDecomposition // using new solver syntax: motionU { solver PCG; preconditioner DIC; tolerance 1e-06; relTol 0; } Selecting motion diffusivity: quadratic // using new solver syntax: U { solver PCG; preconditioner DIC; tolerance 1e-09; relTol 0.01; } Reading transportProperties Reading field p Reading field U Reading/calculating face flux field phi Selecting incompressible transport model Newtonian Selecting turbulence model type RASModel Selecting RAS turbulence model realizableKE realizableKECoeffs { Cmu 0.09; A0 4; C2 1.9; sigmak 1; sigmaEps 1.2; } Reading field U Reading mechanical properties Normalising E : E/rho Calculating Lame's coefficients Plane Stress mu = 9.60735e+06 Pa lambda = 9.46396e+06 Pa Reading coupling properties Starting time loop Courant Number mean: 0 max: 0.000205494 velocity magnitude: 0.286 deltaT = 1.19999e-06 Time = 2.19999e-06 Setting pressure Total pressure force = (0 0 0) DICPCG: Solving for Ux, Initial residual = 0, Final residual = 0, No Iterations 0 DICPCG: Solving for Uy, Initial residual = 0, Final residual = 0, No Iterations 0 DICPCG: Solving for motionUx, Initial residual = 0, Final residual = 0, No Iterations 0 DICPCG: Solving for motionUy, Initial residual = 0, Final residual = 0, No Iterations 0 DICPCG: Solving for motionUx, Initial residual = 0, Final residual = 0, No Iterations 0 DICPCG: Solving for motionUy, Initial residual = 0, Final residual = 0, No Iterations 0 volume continuity errors : volume = 0.000236435, max error = 0, sum local = 0, global = 0 Motion magnitude: mean = 0 max = 0 DILUPBiCG: Solving for Ux, Initial residual = 1, Final residual = 1.05423e-09, No Iterations 1 DILUPBiCG: Solving for Uy, Initial residual = 1, Final residual = 3.21083e-10, No Iterations 1 DICPCG: Solving for p, Initial residual = 1, Final residual = 8.24415e-07, No Iterations 254 DICPCG: Solving for p, Initial residual = 0.028181, Final residual = 9.13188e-07, No Iterations 230 Moving mesh time step continuity errors : sum local = 2.3574e-10, global = -4.60078e-13, cumulative = -4.60078e-13 DICPCG: Solving for p, Initial residual = 0.00804306, Final residual = 8.90858e-07, No Iterations 223 DICPCG: Solving for p, Initial residual = 0.00473995, Final residual = 9.3184e-07, No Iterations 216 Moving mesh time step continuity errors : sum local = 2.64889e-10, global = -1.6892e-12, cumulative = -2.14928e-12 DILUPBiCG: Solving for epsilon, Initial residual = 0.000179671, Final residual = 2.3196e-10, No Iterations 1 DILUPBiCG: Solving for k, Initial residual = 1, Final residual = 1.23968e-08, No Iterations 2 ExecutionTime = 1.01 s End // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // As I am new user of OpenFoam I do not know where is the problem. I thank you in advance for your help. Best Regards, Charbel. |
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March 8, 2011, 07:57 |
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#2 |
Member
Martin
Join Date: Aug 2010
Location: Germany
Posts: 55
Rep Power: 16 |
Dear Charbel,
i do not know about this solver. Normally, if calculation crashes it will write out an error message. Did you already check the endTime entry in controlDict (can be found in the system directory)? With entries in the controlDict, you can specify where to start and to end the calculation and also specify the timeStep. |
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March 8, 2011, 09:23 |
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#3 |
New Member
Charbel Habchi
Join Date: Jan 2011
Location: Lebanon
Posts: 27
Rep Power: 15 |
Dear RugbyGandalf,
Thank you. In fact, I do not think that the controlDict poses problem as you can see it below: // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // application pisoFoam; startFrom startTime; startTime 0; stopAt endTime; endTime 20; deltaT 0.000001; writeControl adjustableRunTime; writeInterval 0.02; purgeWrite 0; writeFormat ascii; writePrecision 6; writeCompression compressed; timeFormat general; timePrecision 6; runTimeModifiable yes; adjustTimeStep yes; maxCo 0.5; // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // I think the problem is more in one of the attached files that you can also find in http://dl.free.fr/azoxbwmku Maybe I made some mistake while trying to built the solver! Best regards, Charbel. |
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March 9, 2011, 05:30 |
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#4 |
Member
Martin
Join Date: Aug 2010
Location: Germany
Posts: 55
Rep Power: 16 |
Dear Charbel,
you're right, that wont cause any problems. I was just overflying the problem and that was my first idea... Maybe someone knows about the mistakes in your files :? I am sorry, but at the time I am hardly in stress, cause of writing exams and a thesis Good luck! |
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March 9, 2011, 07:43 |
corrections for pisoFsiFoam
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#5 |
New Member
Charbel Habchi
Join Date: Jan 2011
Location: Lebanon
Posts: 27
Rep Power: 15 |
Hi,
I found some errors in solveFluid.H that are now corrected in the attached file below. The simulations run now but crashes after some time steps showing large courant number. I will try to see the problem. I have a question remain, in solveFluid.H what most I use: U -= fvc::grad(p)/UEqn.A() or U -= rUA*fvc::grad(p) Can you help please!! Best regards, Charbel. |
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March 23, 2011, 09:52 |
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#6 |
Senior Member
Join Date: Sep 2010
Posts: 226
Rep Power: 17 |
Dear Charbel, kifak mnee7,
look here Ai Ui = Ri--------> solve(UEqn == -fvc::grad(p)) aP-------------------> AU=UEqn().A() U = (1/aP) H[U ]-----> U=UEqn().H()/AU φ = S · H[U ]----------> phi=vc::interpolate(U)& mesh.Sf() ∇ · ( a1 ∇p) = ∇ · (φ) -----> fvm::laplacian(1.0/AU, p)==fvc::div(phi) U = U − (1/aP) ∇p ---------> U-=fvc::grad(p)/AU and we know also volScalarField rUA = 1.0/UEqn.A(); so fvc::grad(p)/UEqn.A() is a vector (grad(p)) times scalar (1/UEqn.A()) where the latter is equal to rUA so vector x scalar = scalar x vector (commutative) so the same. even if it was in matrix form. Best Regards, T.D. |
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March 24, 2011, 03:27 |
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#7 |
New Member
Charbel Habchi
Join Date: Jan 2011
Location: Lebanon
Posts: 27
Rep Power: 15 |
Hello Talib,
Thank you |
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March 24, 2011, 04:10 |
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#8 |
Senior Member
Join Date: Sep 2010
Posts: 226
Rep Power: 17 |
you are welcome
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