 |
 |
 |
|
|
|
[Sponsors] | ||||
bubbleFoam kEpsilon not converging for k on tutorial case |
 |
|
|
LinkBack | Thread Tools | Search this Thread | Display Modes |
March 29, 2013, 13:07
|
bubbleFoam kEpsilon not converging for k on tutorial case
|
#1 |
|
Member
Chris L
Join Date: Sep 2012
Posts: 53
Rep Power: 13  |
Hi all,
EDIT: OF version 2.1.1 run on Ubuntu 12.10 64-bit EDIT2: Using bubbleFoam solver with adjusting time steps and max Courant number of 0.1 (as shown in files) I've been trying to get a simple turbulent case for the bubble column tutorial to work. Any insight would be appreciated. Aside from RASProperties, controlDict, fvSchemes, and fvSolution all other case files are copied from $FOAM_TUTORIALS. Here is the console output showing k as not convergent after 1000 iterations. The final residual for k does not fall within the set tolerance (1e-10) 2 time steps prior to the crash. I'll also attach the complete case file if anyone would like to try to duplicate my results (could always be an isolated issue). Had to split it into 3 files to bypass upload limit. Thanks for your assistance! Code:
Courant Number mean: 0.000102407273185 max: 0.000398086077102
deltaT = 4.60051199094e-06
Time = 2.70030719456e-05
Max Ur Courant Number = 0.000395524440962
DILUPBiCG: Solving for alpha, Initial residual = 4.59536453591e-06, Final residual = 8.49627871868e-14, No Iterations 1
DILUPBiCG: Solving for alpha, Initial residual = 3.64239513162e-10, Final residual = 2.40739677989e-18, No Iterations 1
Dispersed phase volume fraction = 0.367531155235 Min(alpha) = -0.0426521053369 Max(alpha) = 1.00000003097
DICPCG: Solving for p, Initial residual = 0.0162179181138, Final residual = 0.00133310181578, No Iterations 2
time step continuity errors : sum local = 1.01714630608e-07, global = -1.68614375755e-09, cumulative = -1.91330433001e-09
DICPCG: Solving for p, Initial residual = 1.51812125528e-11, Final residual = 1.51812125528e-11, No Iterations 0
time step continuity errors : sum local = 1.46990226886e-06, global = -9.90708097536e-09, cumulative = -1.18203853054e-08
DILUPBiCG: Solving for epsilon, Initial residual = 0.231630236664, Final residual = 8.42668640452e-11, No Iterations 47
DILUPBiCG: Solving for k, Initial residual = 0.999999999966, Final residual = 4.32822169403e-11, No Iterations 25
ExecutionTime = 0.7 s ClockTime = 1 s
Courant Number mean: 0.000123381039631 max: 0.000477693777356
deltaT = 5.52061438912e-06
Time = 3.25236863347e-05
Max Ur Courant Number = 0.00345730592145
DILUPBiCG: Solving for alpha, Initial residual = 7.05319909257e-06, Final residual = 8.14315093719e-14, No Iterations 1
DILUPBiCG: Solving for alpha, Initial residual = 8.98578469072e-10, Final residual = 2.43568983429e-16, No Iterations 1
Dispersed phase volume fraction = 0.367531167119 Min(alpha) = -0.0426027794407 Max(alpha) = 1.00001233594
DICPCG: Solving for p, Initial residual = 0.998693417498, Final residual = 0.0801310279758, No Iterations 1
time step continuity errors : sum local = 9452829.84033, global = -233370.797544, cumulative = -233370.797544
DICPCG: Solving for p, Initial residual = 0.981382974041, Final residual = 9.55331203874e-11, No Iterations 97
time step continuity errors : sum local = 0.000920508954439, global = 7.95903751645e-06, cumulative = -233370.797536
DILUPBiCG: Solving for epsilon, Initial residual = 0.132690637905, Final residual = 2.2112305474e-11, No Iterations 51
DILUPBiCG: Solving for k, Initial residual = 0.999953338395, Final residual = 1.10353183522e-05, No Iterations 1001
ExecutionTime = 0.82 s ClockTime = 1 s
Courant Number mean: 141650.102468 max: 19724594.6518
deltaT = 2.79884808108e-14
Time = 3.25236863627e-05
Max Ur Courant Number = 0.0994415796924
DILUPBiCG: Solving for alpha, Initial residual = 2.45599764286e-06, Final residual = 1.28886564037e-13, No Iterations 2
DILUPBiCG: Solving for alpha, Initial residual = 3.51283163256e-09, Final residual = 1.55146580667e-12, No Iterations 1
Dispersed phase volume fraction = 0.367531167118 Min(alpha) = -0.0426027794358 Max(alpha) = 1.00001190501
DICPCG: Solving for p, Initial residual = 0.99979819169, Final residual = 0.0993892919159, No Iterations 4
time step continuity errors : sum local = 4.14687054711e-05, global = 4.10543983161e-05, cumulative = -233370.797495
DICPCG: Solving for p, Initial residual = 9.15918445237e-13, Final residual = 9.15918445237e-13, No Iterations 0
time step continuity errors : sum local = 31421.2935774, global = 1.0089083647e-05, cumulative = -233370.797485
DILUPBiCG: Solving for epsilon, Initial residual = 0.334698297328, Final residual = 6.94339113676e-11, No Iterations 49
DILUPBiCG: Solving for k, Initial residual = 0.999999999994, Final residual = 3067812984.81, No Iterations 1001
ExecutionTime = 0.94 s ClockTime = 1 s
Courant Number mean: 15907.1845113 max: 8059028.69188
deltaT = 3.47293475192e-22
--> FOAM Warning :
From function Time::operator++()
in file db/Time/Time.C at line 1010
Increased the timePrecision from 12 to 13 to distinguish between timeNames at time 3.25236863627e-05
Time = 3.252368636273e-05
Max Ur Courant Number = 0.19986730275
DILUPBiCG: Solving for alpha, Initial residual = 0.000616348386473, Final residual = 5.50418899126e-12, No Iterations 1
DILUPBiCG: Solving for alpha, Initial residual = 9.60748786488e-05, Final residual = 1.0790473386e-13, No Iterations 1
Dispersed phase volume fraction = 0.367531167118 Min(alpha) = -0.0426027794358 Max(alpha) = 1.13514811002
DICPCG: Solving for p, Initial residual = 0.0275952712201, Final residual = 0.00258600645723, No Iterations 1
time step continuity errors : sum local = 0.000828517498979, global = 2.72132533698e-06, cumulative = -233370.797482
DICPCG: Solving for p, Initial residual = 2.34594789529e-11, Final residual = 2.34594789529e-11, No Iterations 0
time step continuity errors : sum local = 7.29578945652e+64, global = -1.72643961598e+41, cumulative = -1.72643961598e+41
#0 Foam::error::printStack(Foam::Ostream&) at ??:?
#1 Foam::sigFpe::sigHandler(int) at ??:?
#2 in "/lib/x86_64-linux-gnu/libc.so.6"
#3 Foam::PBiCG::solve(Foam::Field<double>&, Foam::Field<double> const&, unsigned char) const at ??:?
#4 Foam::fvMatrix<double>::solve(Foam::dictionary const&) at ??:?
#5
at ??:?
#6
at ??:?
#7 __libc_start_main in "/lib/x86_64-linux-gnu/libc.so.6"
#8
at ??:?
Floating point exception (core dumped)
Code:
/*--------------------------------*- C++ -*----------------------------------*\
| ========= | |
| \\ / F ield | OpenFOAM: The Open Source CFD Toolbox |
| \\ / O peration | Version: 2.1.1 |
| \\ / A nd | Web: www.OpenFOAM.org |
| \\/ M anipulation | |
\*---------------------------------------------------------------------------*/
FoamFile
{
version 2.0;
format ascii;
class dictionary;
location "constant";
object RASProperties;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
RASModel kEpsilon;
turbulence on;
printCoeffs on;
// ************************************************************************* //
Code:
/*--------------------------------*- C++ -*----------------------------------*\
| ========= | |
| \\ / F ield | OpenFOAM: The Open Source CFD Toolbox |
| \\ / O peration | Version: 2.1.1 |
| \\ / A nd | Web: www.OpenFOAM.org |
| \\/ M anipulation | |
\*---------------------------------------------------------------------------*/
FoamFile
{
version 2.0;
format ascii;
class dictionary;
location "system";
object controlDict;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
application bubbleFoam;
startFrom startTime;
startTime 0;
stopAt endTime;
endTime 20;
deltaT 0.0000001;
writeControl runTime;
writeInterval 0.5;
purgeWrite 0;
writeFormat ascii;
writePrecision 12;
writeCompression uncompressed;
timeFormat general;
timePrecision 12;
runTimeModifiable yes;
adjustTimeStep yes;
maxCo 0.1;
maxAlphaCo 0.1;
maxDeltaT 0.01;
// ************************************************************************* //
Code:
/*--------------------------------*- C++ -*----------------------------------*\
| ========= | |
| \\ / F ield | OpenFOAM: The Open Source CFD Toolbox |
| \\ / O peration | Version: 2.1.1 |
| \\ / A nd | Web: www.OpenFOAM.org |
| \\/ M anipulation | |
\*---------------------------------------------------------------------------*/
FoamFile
{
version 2.0;
format ascii;
class dictionary;
location "system";
object fvSchemes;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
ddtSchemes
{
default Euler;
}
gradSchemes
{
default Gauss linear;
}
divSchemes
{
default none;
div(phia,Ua) Gauss limitedLinearV 1;
div(phib,Ub) Gauss limitedLinearV 1;
div(phib,k) Gauss limitedLinear 1;
div(phib,epsilon) Gauss limitedLinear 1;
div(phi,alpha) Gauss limitedLinear01 1;
div((-nuEffa*T(grad(Ua)))) Gauss linear;
div((-nuEffb*T(grad(Ub)))) Gauss linear;
}
laplacianSchemes
{
default none;
laplacian(nuEffa,Ua) Gauss linear corrected;
laplacian(nuEffb,Ub) Gauss linear corrected;
laplacian((rho*(1|A(U))),p) Gauss linear corrected;
laplacian(DepsilonEff,epsilon) Gauss linear corrected;
laplacian(DkEff,k) Gauss linear corrected;
}
interpolationSchemes
{
default linear;
}
snGradSchemes
{
default corrected;
}
fluxRequired
{
default no;
p ;
}
// ************************************************************************* //
Code:
/*--------------------------------*- C++ -*----------------------------------*\
| ========= | |
| \\ / F ield | OpenFOAM: The Open Source CFD Toolbox |
| \\ / O peration | Version: 2.1.1 |
| \\ / A nd | Web: www.OpenFOAM.org |
| \\/ M anipulation | |
\*---------------------------------------------------------------------------*/
FoamFile
{
version 2.0;
format ascii;
class dictionary;
location "system";
object fvSolution;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
solvers
{
p
{
solver PCG;
preconditioner DIC;
tolerance 1e-10;
relTol 0.1;
}
pFinal
{
$p;
tolerance 1e-10;
relTol 0;
}
alpha
{
solver PBiCG;
preconditioner DILU;
tolerance 1e-10;
relTol 0.1;
}
alphaFinal
{
$alpha;
tolerance 1e-10;
relTol 0;
}
k
{
solver PBiCG;
preconditioner DILU;
tolerance 1e-10;
relTol 0;
}
epsilon
{
solver PBiCG;
preconditioner DILU;
tolerance 1e-10;
relTol 0;
}
kFinal
{
$alpha;
tolerance 1e-10;
relTol 0;
}
epsilonFinal
{
$alpha;
tolerance 1e-10;
relTol 0;
}
}
PIMPLE
{
nCorrectors 2;
nNonOrthogonalCorrectors 0;
nAlphaCorr 2;
correctAlpha no;
pRefCell 0;
pRefValue 0;
}
// ************************************************************************* //
Last edited by vbchris; March 30, 2013 at 13:26. |
|
|
|
|
|
March 31, 2013, 23:45
|
|
#2 |
|
Member
Chris L
Join Date: Sep 2012
Posts: 53
Rep Power: 13 |
As a follow-up:
I've also attempted various tolerances for k and epsilon. The blow-up has been duplicated this on a separate machine. Various BCs have been attempted including zeroGrad for outlets instead of inletOutlet for all variables (except p). The mesh was re-built and a different mesh was tested. I assume at the point that I have overlooked something obvious. Thanks, |
|
|
|
|
|
|
|
|
Similar Threads
|
||||
| Thread | Thread Starter | Forum | Replies | Last Post |
| Pressure instabilities with interDyMFoam for the floatingObject case | nbadano | OpenFOAM Running, Solving & CFD | 15 | October 15, 2021 06:35 |
| 0.org directory bubbleFoam tutorial | matt.mech.eng | OpenFOAM | 3 | March 1, 2012 04:17 |
| case and dat file of FLUENT tutorial | Sajad Ranjbaran | FLUENT | 0 | November 8, 2006 06:55 |
| Free surface boudary conditions with SOLA-VOF | Fan | Main CFD Forum | 10 | September 9, 2006 12:24 |
| Case in Fluent Tutorial 1 | Lam | FLUENT | 0 | August 24, 2004 11:25 |
Linear Mode
