CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > OpenFOAM > OpenFOAM Running, Solving & CFD

Convergence Problem icoFoam steady flow over an airfoil

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   January 5, 2011, 22:18
Default Convergence Problem icoFoam steady flow over an airfoil
  #1
New Member
 
Lucas Vieira
Join Date: Nov 2010
Posts: 6
Rep Power: 16
Lucas is on a distinguished road
Hi everyone,

I am trying to simulate steady flow over an airfoil and I'm having problems converging to the solution with icoFoam.

I'm using a ICEM mesh that i exported to fluent format (msh) and converted with
fluentMesh3DToFoam:

I am working with a comparation between OpenFOAM and CFX,
but i am new at OF.

The utility checkMesh set Mesh OK.

This is my case:
http://uploaddearquivos.com.br/downl...o/PROIC.tar.gz

Thank you.
Lucas is offline   Reply With Quote

Old   January 6, 2011, 09:49
Default
  #2
New Member
 
Lucas Vieira
Join Date: Nov 2010
Posts: 6
Rep Power: 16
Lucas is on a distinguished road
I tried this morning some changes in the fvschemes fvsolution
I also tried to run in simpleFoam

and i got this:

Code:
 Time = 52

Lookup gradScheme for grad(U)
Lookup divScheme for div((nuEff*dev(grad(U).T())))
Lookup laplacianScheme for laplacian(nuEff,U)
Lookup fluxRequired for U
Lookup gradScheme for snGradCorr(U)
Lookup gradScheme for snGradCorr(U)
Lookup gradScheme for snGradCorr(U)
Lookup divScheme for div(phi,U)
Find relax for U
Lookup relaxationFactor for U
Lookup gradScheme for grad(p)

    From function solution::solverDict(const word&)
    in file matrices/solution/solution.C at line 241
    Lookup solver for U
smoothSolver:  Solving for Ux, Initial residual = 0.0237871, Final residual = 0.000128133, No Iterations 1
smoothSolver:  Solving for Uy, Initial residual = 0.317853, Final residual = 0.00208853, No Iterations 1
smoothSolver:  Solving for Uz, Initial residual = 8.9633e-05, Final residual = 4.39538e-07, No Iterations 1
Lookup interpolationScheme for interpolate(U)


--> FOAM FATAL ERROR: 
Continuity error cannot be removed by adjusting the outflow.
Please check the velocity boundary conditions and/or run potentialFoam to initialise the outflow.
Total flux              : 3.36963e+38
Specified mass inflow   : 1.60459e+38
Specified mass outflow  : 0
Adjustable mass outflow : 4.20186e+20


    From function adjustPhi(surfaceScalarField& phi, const volVectorField& U,const volScalarField& p
    in file cfdTools/general/adjustPhi/adjustPhi.C at line 115.

FOAM exiting
hear is my system files:

Code:
/*--------------------------------*- C++ -*----------------------------------*\
| =========                 |                                                 |
| \\      /  F ield         | OpenFOAM: The Open Source CFD Toolbox           |
|  \\    /   O peration     | Version:  1.7.1                                 |
|   \\  /    A nd           | Web:      www.OpenFOAM.com                      |
|    \\/     M anipulation  |                                                 |
\*---------------------------------------------------------------------------*/
FoamFile
{
    version     2.0;
    format      ascii;
    class       dictionary;
    location    "system";
    object      controlDict;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //

application     simpleFoam;   //  which solver (for documentation)

startFrom       startTime;              //  firstTime, startTime, latestTime

startTime       0;                      //  set > 0 to continue

stopAt          endTime;                //  writeNow, endTime, nextWrite, ...

endTime         600;                    //  Latest timestep allowed

deltaT          1;                      //  simple counter for steadyState

writeControl    adjustableRunTime;      //  or uncommon: cpuTime, clockTime

writeInterval   50;                     //  time step write interval

purgeWrite      0;                      //  1 recycles time steps storage
                                        //  0 keeps all time steps on disk

writeFormat     ascii;                  //  ascii: readable, binary: smaller

writePrecision  6;                      //  precision for ascii format

writeCompression uncompressed;          //  compressed for gzipped files

timeFormat      general;                //  fixed, scientific or general

timePrecision   6;                      //  precision for time handling

runTimeModifiable yes;                  //  yes: OF reads dictionaries each
                                        //  time step

graphFormat     raw;                    //  raw, gnuplot, xmgr, jplot

//libs()        for user libraries, p.e. user boundary conditions
//functions()   for special functions
Code:
/*--------------------------------*- C++ -*----------------------------------*\
| =========                 |                                                 |
| \\      /  F ield         | OpenFOAM: The Open Source CFD Toolbox           |
|  \\    /   O peration     | Version:  1.7.1                                 |
|   \\  /    A nd           | Web:      www.OpenFOAM.com                      |
|    \\/     M anipulation  |                                                 |
\*---------------------------------------------------------------------------*/
FoamFile
{
    version     2.0;
    format      ascii;
    class       dictionary;
    location    "system";
    object      fvSchemes;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //

ddtSchemes
{
    default         steadyState;
}

gradSchemes
{
    default         Gauss linear;
    grad(p)         faceLimited leastSquares 0 1;
    grad(U)         Gauss linear;
}

divSchemes
{
    default         none;
    div(phi,U)      Gauss upwind;
    div(phi,nuTilda) Gauss linearUpwind Gauss linear;
    div((nuEff*dev(grad(U).T()))) Gauss linear;
}

laplacianSchemes
{
    default         none;
    laplacian(nuEff,U) Gauss linear limited 0.7;
    laplacian((1|A(U)),p) Gauss linear limited 0.7;
    laplacian(DnuTildaEff,nuTilda) Gauss linear corrected;
    laplacian(1,p)  Gauss linear corrected;
}

interpolationSchemes
{
    default         linear;
    interpolate(U)  linear;
}

snGradSchemes
{
    default         limited 0.7;
}

fluxRequired
{
    default         no;
    p               ;
}


// ************************************************************************* //
Code:
/*--------------------------------*- C++ -*----------------------------------*\
| =========                 |                                                 |
| \\      /  F ield         | OpenFOAM: The Open Source CFD Toolbox           |
|  \\    /   O peration     | Version:  1.7.1                                 |
|   \\  /    A nd           | Web:      www.OpenFOAM.com                      |
|    \\/     M anipulation  |                                                 |
\*---------------------------------------------------------------------------*/
FoamFile
{
    version     2.0;
    format      ascii;
    class       dictionary;
    location    "system";
    object      fvSolution;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //

solvers
{
    p
    {
        solver          GAMG;
        tolerance       1e-07;
        relTol          0.001;
        smoother        GaussSeidel;
        nPreSweeps      1;
        nPostSweeps     2;
        cacheAgglomeration true;
        nCellsInCoarsestLevel 500;
        agglomerator    faceAreaPair;
        mergeLevels     1;
    }

    U
    {
        solver          smoothSolver;
        smoother        GaussSeidel;
        nSweeps         2;
        tolerance       1e-08;
        relTol          0.01;
    nSweeps         1;              // setting for smoothSolver
        maxIter         100;            // limitation of iterations number

    }

    nuTilda
    {
        solver          smoothSolver;
        smoother        GaussSeidel;
        nSweeps         2;
        tolerance       1e-08;
        relTol          0.1;
    }
}

SIMPLE
{
    nNonOrthogonalCorrectors 6;
    convergence         1e-5;
    pRefCell        0;
    pRefValue       0;
}

relaxationFactors
{
    default         0;
    p               0.003;
    U               0.007;
    nuTilda         0.007;
}


// ************************************************************************* //
Lucas is offline   Reply With Quote

Old   January 6, 2011, 12:08
Default
  #3
Senior Member
 
Travis Carrigan
Join Date: Jul 2010
Location: Arlington, TX
Posts: 161
Rep Power: 16
tcarrigan is on a distinguished road
For the gradSchemes try:
default cellLimited leastSquares 1.0;

For the divSchemes try:
div(phi,U) Gauss linearUpwindV Gauss linear;
div(phi,nuTilda) Gauss upwind;

For pressure solver:
p GAMG tolerance 1e-8 and relTol 0

For other solvers:
PBiCG using DILU preconditioner with tolerances 1e-8 and relTol 0 rather than using smoothSolver

Try also dropping the nNonOrthogonalCorrectors down to 2, and increase the relaxation factors:
p 0.2
U 0.5
nuTilda 0.5
tcarrigan is offline   Reply With Quote

Old   January 10, 2011, 15:24
Default
  #4
New Member
 
Lucas Vieira
Join Date: Nov 2010
Posts: 6
Rep Power: 16
Lucas is on a distinguished road
thanks for your reply, but the problem was the mesh, i changed the mesh and
everything works fine.
Lucas is offline   Reply With Quote

Old   February 17, 2011, 18:24
Default
  #5
Member
 
William
Join Date: Feb 2011
Location: Minnesota USA
Posts: 33
Rep Power: 15
billynoe is on a distinguished road
Quote:
Originally Posted by Lucas View Post
thanks for your reply, but the problem was the mesh, i changed the mesh and
everything works fine.
what did you change in your mesh? smaller cell sizes?
billynoe is offline   Reply With Quote

Old   February 18, 2011, 13:46
Default
  #6
New Member
 
Lucas Vieira
Join Date: Nov 2010
Posts: 6
Rep Power: 16
Lucas is on a distinguished road
In fact i made a complete new mesh, because the last was horrible, with high number of non-orthogonal cells.
Lucas is offline   Reply With Quote

Old   July 12, 2018, 16:06
Default Convergence
  #7
Member
 
Ben 017
Join Date: Nov 2017
Posts: 70
Rep Power: 9
Ben UWIHANGANYE is on a distinguished road
Hello Foamers,

referring to the attached residuals plot, is it possible to conclude that my simulation has converged at 300th iteration or i am wrong?

Can You advise how to evaluate the convergence of my simulation?

I am simulating flow past an immersed cylinder using icoDyMIbFOAM in foam-extend 4.0

I will be happy to get your feedback.

Regard!

Ben
Attached Images
File Type: png icofoam residuals.png (23.0 KB, 9 views)
Ben UWIHANGANYE is offline   Reply With Quote

Reply


Posting Rules
You may not post new threads
You may not post replies
You may not post attachments
You may not edit your posts

BB code is On
Smilies are On
[IMG] code is On
HTML code is Off
Trackbacks are Off
Pingbacks are On
Refbacks are On


Similar Threads
Thread Thread Starter Forum Replies Last Post
Convergence Problem with two phase flow challenger85 CFX 0 December 29, 2009 09:01
Convergence Problem with body force driven flow Jinfeng FLUENT 1 December 9, 2009 04:54
initialization of flow field to enhance convergence rate to steady state vfico Main CFD Forum 0 September 9, 2009 12:23
Convergence problem for compressible flow Saad Main CFD Forum 2 June 5, 2005 16:24
Turbulent steady flow around a circular cylinder Mirek Kabacinski FLUENT 0 July 23, 2003 19:40


All times are GMT -4. The time now is 19:20.