Revision as of 17:37, 6 January 2019

SimpleFoam

SimpleFoam is a steady-state solver for incompressible, turbulent flow, using the SIMPLE (Semi-Implicit Method for Pressure Linked Equations) algorithm. In the newer releases it also includes an option to use the SIMPLEC (Semi-Implicit Method for Pressure Linked Equations Consistent) algorithm.

1 Solution Strategy

The solver follows a segregated solution strategy. This means that the equations for each variable characterizing the system (the velocity $\bold u$ , the pressure $p$ and the variables characterizing turbulence) is solved sequentially and the solution of the preceding equations is inserted in the subsequent equation. The non-linearity appearing in the momentum equation (the face flux $\phi_f$ which is a function of the velocity) is resolved by computing it from the velocity and pressure values of the preceding iteration. The dependence from the pressure is introduced to avoid a decoupling between the momentum and pressure equations and hence the appearance of high frequency oscillation in the solution (check board effect). The first equation to be solve is the momentum equation. It delivers a velocity field $\bold u^*$ which is in general not divergence free, i.e. it does not satisfy the continuity equation. After that the momentum and the continuity equations are used to construct an equation for the pressure. The aim is to obtain a pressure field $p^{n}$ , which, if inserted in the momentum equation, delivers a divergence free velocity field $\bold u$ . After correcting the velocity field, the equations for turbulence are solved. The above iterative solution procedure is repeated until convergence.

The source code can be found in simpleFoam.C

 
 
/*---------------------------------------------------------------------------*\
  =========                 |
  \\      /  F ield         | OpenFOAM: The Open Source CFD Toolbox
   \\    /   O peration     | Website:  https://openfoam.org
    \\  /    A nd           | Copyright (C) 2011-2018 OpenFOAM Foundation
     \\/     M anipulation  |
-------------------------------------------------------------------------------
License
    This file is part of OpenFOAM.
 
    OpenFOAM is free software: you can redistribute it and/or modify it
    under the terms of the GNU General Public License as published by
    the Free Software Foundation, either version 3 of the License, or
    (at your option) any later version.
 
    OpenFOAM is distributed in the hope that it will be useful, but WITHOUT
    ANY WARRANTY; without even the implied warranty of MERCHANTABILITY or
    FITNESS FOR A PARTICULAR PURPOSE.  See the GNU General Public License
    for more details.
 
    You should have received a copy of the GNU General Public License
    along with OpenFOAM.  If not, see <http://www.gnu.org/licenses/>.
 
Application
    simpleFoam
 
Description
    Steady-state solver for incompressible, turbulent flow, using the SIMPLE
    algorithm.
 
\*---------------------------------------------------------------------------*/
 
#include "fvCFD.H"
#include "singlePhaseTransportModel.H"
#include "turbulentTransportModel.H"
#include "simpleControl.H"
#include "fvOptions.H"
 
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
 
int main(int argc, char *argv[])
{
    #include "postProcess.H"
 
    #include "setRootCaseLists.H"
    #include "createTime.H"
    #include "createMesh.H"
    #include "createControl.H"
    #include "createFields.H"
    #include "initContinuityErrs.H"
 
    turbulence->validate();
 
    // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
 
    Info<< "\nStarting time loop\n" << endl;
 
    while (simple.loop(runTime))
    {
        Info<< "Time = " << runTime.timeName() << nl << endl;
 
        // --- Pressure-velocity SIMPLE corrector
        {
            #include "UEqn.H"
            #include "pEqn.H"
        }
 
        laminarTransport.correct();
        turbulence->correct();
 
        runTime.write();
 
        Info<< "ExecutionTime = " << runTime.elapsedCpuTime() << " s"
            << "  ClockTime = " << runTime.elapsedClockTime() << " s"
            << nl << endl;
    }
 
    Info<< "End\n" << endl;
 
    return 0;
}
 
 
// ************************************************************************* //

2 Equations

2.1 Momentum Equation

\frac{\partial \left( {u}_j u_i \right) }{\partial x_j}= - \frac{1}{\rho}\frac{\partial p} {\partial{x_i}} + \frac{1}{\rho}\frac{\partial}{\partial x_j} \left( \tau_{ij} + \tau_{t_{ij}} \right)

(1)

$u$ represent the velocity and $\tau_{ij}$ and $\tau_{t_{ij}}$ are the viscose and turbulent stresses. Not that in simpleFoam the momentum equation solve, is divided by the constant density $\rho$ .

The source code can be found in UEqn.H:

 
 
        // Momentum predictor
 
    MRF.correctBoundaryVelocity(U);
 
    tmp<fvVectorMatrix> tUEqn
    (
        fvm::div(phi, U)
      + MRF.DDt(U)
      + turbulence->divDevReff(U)
     ==
        fvOptions(U)
    );
    fvVectorMatrix& UEqn = tUEqn.ref();
 
    UEqn.relax();
 
    fvOptions.constrain(UEqn);
 
    if (simple.momentumPredictor())
    {
        solve(UEqn == -fvc::grad(p));
 
        fvOptions.correct(U);
    }

In the following the numeric used to solve the momentum equation are briefly explained. The first step performed is to assemble the matrix which is later solved to obtain the estimate of the velocity $\bold u^*$ :

 
    tmp<fvVectorMatrix> tUEqn
    (
        fvm::div(phi, U)
      + MRF.DDt(U)
      + turbulence->divDevReff(U)
     ==
        fvOptions(U)
    );

In the usual semi discrete form it can be written as (see also ^[1]. ):

\bold{a_P u_P} + \sum_{N} \bold{a_N u_N} = \bold b_P

(1)

$\bold a_P$ are the matrix coefficient associated with the centre point P, $\bold a_N$ the matrix coefficients associated with all neighbours influencing the computational stencil around point P and $\bold b_P$ is the source therm. The sum $\sum_N$ is taken over all neighbours influencing the computational stencil around point P.

The next step performed is the under relax the equation:

 
    UEqn.relax();

 The under relaxation is required in order to prevent the solution to diverge. Even though the discrete equation of the momentum

equation is linear, the non linearity is resolve by using the solution of the previous iteration. This causes a large change of the new velocity leading often to divergence ^[2]. Using Patankar's implicit under relaxation the new semi discrete momentum equation can be written as:

\frac{1}{\alpha}\bold{a_P u_P} + \sum_{N} \bold{a_N u_N} = \bold b_P + \frac{1 - \alpha}{\alpha}\bold{a_P u_P}^{n-1}

(1)

Here $\alpha$ denotes the under relaxation factor and $\bold{u_P}^{n-1}$ denotes the solution at the previous iteration step. The source code for the under relaxation can be found in fvMatrix.C (see also https://www.openfoam.com/documentation/cpp-guide/html/fvMatrix_8C_source.html):

 
 
   template<class Type>
 void Foam::fvMatrix<Type>::relax(const scalar alpha)
 {
     if (alpha <= 0)
     {
         return;
     }
 
     if (debug)
     {
         InfoInFunction
             << "Relaxing " << psi_.name() << " by " << alpha << endl;
     }
 
     Field<Type>& S = source();
     scalarField& D = diag();
 
     // Store the current unrelaxed diagonal for use in updating the source
     scalarField D0(D);
 
     // Calculate the sum-mag off-diagonal from the interior faces
     scalarField sumOff(D.size(), 0.0);
     sumMagOffDiag(sumOff);
 
     // Handle the boundary contributions to the diagonal
     forAll(psi_.boundaryField(), patchi)
     {
         const fvPatchField<Type>& ptf = psi_.boundaryField()[patchi];
 
         if (ptf.size())
         {
             const labelUList& pa = lduAddr().patchAddr(patchi);
             Field<Type>& iCoeffs = internalCoeffs_[patchi];
 
             if (ptf.coupled())
             {
                 const Field<Type>& pCoeffs = boundaryCoeffs_[patchi];
 
                 // For coupled boundaries add the diagonal and
                 // off-diagonal contributions
                 forAll(pa, face)
                 {
                     D[pa[face]] += component(iCoeffs[face], 0);
                     sumOff[pa[face]] += mag(component(pCoeffs[face], 0));
                 }
             }
             else
             {
                 // For non-coupled boundaries add the maximum magnitude diagonal
                 // contribution to ensure stability
                 forAll(pa, face)
                 {
                     D[pa[face]] += cmptMax(cmptMag(iCoeffs[face]));
                 }
             }
         }
     }
 
 
     if (debug)
     {
         // Calculate amount of non-dominance.
         label nNon = 0;
         scalar maxNon = 0.0;
         scalar sumNon = 0.0;
         forAll(D, celli)
         {
             scalar d = (sumOff[celli] - D[celli])/mag(D[celli]);
 
             if (d > 0)
             {
                 nNon++;
                 maxNon = max(maxNon, d);
                 sumNon += d;
             }
         }
 
         reduce(nNon, sumOp<label>(), UPstream::msgType(), psi_.mesh().comm());
         reduce
         (
             maxNon,
             maxOp<scalar>(),
             UPstream::msgType(),
             psi_.mesh().comm()
         );
         reduce
         (
             sumNon,
             sumOp<scalar>(),
             UPstream::msgType(),
             psi_.mesh().comm()
         );
         sumNon /= returnReduce
         (
             D.size(),
             sumOp<label>(),
             UPstream::msgType(),
             psi_.mesh().comm()
         );
 
         InfoInFunction
             << "Matrix dominance test for " << psi_.name() << nl
             << "    number of non-dominant cells   : " << nNon << nl
             << "    maximum relative non-dominance : " << maxNon << nl
             << "    average relative non-dominance : " << sumNon << nl
             << endl;
     }
 
 
     // Ensure the matrix is diagonally dominant...
     // Assumes that the central coefficient is positive and ensures it is
     forAll(D, celli)
     {
         D[celli] = max(mag(D[celli]), sumOff[celli]);
     }
 
     // ... then relax
     D /= alpha;
 
     // Now remove the diagonal contribution from coupled boundaries
     forAll(psi_.boundaryField(), patchi)
     {
         const fvPatchField<Type>& ptf = psi_.boundaryField()[patchi];
 
         if (ptf.size())
         {
             const labelUList& pa = lduAddr().patchAddr(patchi);
             Field<Type>& iCoeffs = internalCoeffs_[patchi];
 
             if (ptf.coupled())
             {
                 forAll(pa, face)
                 {
                     D[pa[face]] -= component(iCoeffs[face], 0);
                 }
             }
             else
             {
                 forAll(pa, face)
                 {
                     D[pa[face]] -= cmptMin(iCoeffs[face]);
                 }
             }
         }
     }
 
     // Finally add the relaxation contribution to the source.
     S += (D - D0)*psi_.primitiveField();
 }

After the under relaxation the contribution of the pressure gradient is added to the right hand side of the matrix and the system is solve:

 
        solve(UEqn == -fvc::grad(p));

The equation in semi discrete form looks as follows:

\frac{1}{\alpha}\bold{a_P u_P} + \sum_{N} \bold{a_N u_N} = \bold b_P + \frac{1 - \alpha}{\alpha}\bold{a_P u_P}^{n-1} + \nabla p_P

(1)

$\nabla p_p$ denotes the contribution of the pressure gradient to the equation of the cell centre p.

Important for the understanding of the later described pressure equation is that the contribution of the pressure equation is not added to the source therm of the matrix object UEqn. Rather a new fvMatrix object is returned by the call of the overloaded operator == to the function solve:

 
        UEqn == -fvc::grad(p)

The function solve is then executed, which solves the new fvMatrix object in order to obtain the estimate $\bold u^*$ by also considering the contribution of the pressure equation. Note that the the volVectorField U is modified by solving the matrix since the solution vector $\psi$ of the matrix is a reference to U. An explanation of the the implementation can be found also in https://www.cfd-online.com/Forums/openfoam/213566-why-solve-ueqn-fvc-grad-p-ueqn-source-not-modified-ueqn-h-chang.html.

2.2 Pressure Equation

2.3 Equations for the turbulence

3 References

↑ Moukalled, F., L. Mangani, and M. Darwish. "The finite volume method in computational fluid dynamics." An Advanced Introduction with OpenFOAM and Matlab (2016):
↑ Moukalled, F., L. Mangani, and M. Darwish. "The finite volume method in computational fluid dynamics." An Advanced Introduction with OpenFOAM and Matlab (2016):

[1] Moukalled, F., L. Mangani, and M. Darwish. "The finite volume method in computational fluid dynamics." An Advanced Introduction with OpenFOAM and Matlab (2016):

[2] Moukalled, F., L. Mangani, and M. Darwish. "The finite volume method in computational fluid dynamics." An Advanced Introduction with OpenFOAM and Matlab (2016):

[1]

[2]

@@ Line 378: / Line 378: @@
 <math> \nabla p_p </math> denotes the contribution of the pressure gradient to the equation of the cell centre p.
+Important for the understanding of the later described pressure equation is that the contribution of the pressure equation is not added to the source therm of the
+matrix object UEqn. Rather a new fvMatrix object is returned by the call of the overloaded operator ==  to the function solve:
+<br><cpp>
+        UEqn == -fvc::grad(p)
+</cpp><br>
+The function solve is then executed, which solves the new fvMatrix object in order to obtain the estimate <math> \bold u^*</math> by also considering the contribution
+of the pressure equation. Note that the the volVectorField U is modified by solving the matrix since the solution vector <math> \psi </math> of the matrix  is a reference to U.
+An explanation of the the implementation can be found also in https://www.cfd-online.com/Forums/openfoam/213566-why-solve-ueqn-fvc-grad-p-ueqn-source-not-modified-ueqn-h-chang.html.
 ===Pressure Equation===

Difference between revisions of "SimpleFoam"