incompressibleDriftFlux.C

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#include "incompressibleDriftFlux.H"
#include "fvCorrectPhi.H"
#include "addToRunTimeSelectionTable.H"
 
#include "fvmDdt.H"
 
#include "fvcDdt.H"
 
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
 
namespace Foam
{
namespace solvers
{
    defineTypeNameAndDebug(incompressibleDriftFlux, 0);
    addToRunTimeSelectionTable(solver, incompressibleDriftFlux, fvMesh);
}
}
 
 
// * * * * * * * * * * * * * Private Member Functions  * * * * * * * * * * * //
 
void Foam::solvers::incompressibleDriftFlux::correctCoNum()
{
    VoFSolver::correctCoNum();
}
 
 
// * * * * * * * * * * * * * Protected Member Functions  * * * * * * * * * * //
 
void Foam::solvers::incompressibleDriftFlux::setInterfaceRDeltaT
(
    volScalarField& rDeltaT
)
{}
 
 
void Foam::solvers::incompressibleDriftFlux::correctInterface()
{}
 
 
Foam::tmp<Foam::surfaceScalarField>
Foam::solvers::incompressibleDriftFlux::surfaceTensionForce() const
{
    return surfaceScalarField::New
    (
        "surfaceTensionForce",
        mesh,
        dimensionedScalar(dimForce/dimVolume, 0)
    );
}
 
 
// * * * * * * * * * * * * * * * * Constructors  * * * * * * * * * * * * * * //
 
Foam::solvers::incompressibleDriftFlux::incompressibleDriftFlux(fvMesh& mesh)
:
    twoPhaseSolver
    (
        mesh,
        autoPtr<twoPhaseVoFMixture>(new incompressibleDriftFluxMixture(mesh))
    ),
 
    mixture
    (
        refCast<incompressibleDriftFluxMixture>(twoPhaseSolver::mixture)
       .initialise(U)
    ),
 
    p
    (
        IOobject
        (
            "p",
            runTime.name(),
            mesh,
            IOobject::NO_READ,
            IOobject::AUTO_WRITE
        ),
        p_rgh + rho*buoyancy.gh
    ),
 
    pressureReference_
    (
        p,
        p_rgh,
        pimple.dict()
    ),
 
    relativeVelocity
    (
        relativeVelocityModel::New(mixture, mixture, buoyancy.g)
    ),
 
    packingDispersion
    (
        packingDispersionModel::New(mixture, relativeVelocity)
    ),
 
    momentumTransport
    (
        compressible::momentumTransportModel::New(rho, U, rhoPhi, mixture)
    )
{
    if (transient())
    {
        correctCoNum();
    }
 
    if (correctPhi || mesh.topoChanging())
    {
        rAU = new volScalarField
        (
            IOobject
            (
                "rAU",
                runTime.name(),
                mesh,
                IOobject::READ_IF_PRESENT,
                IOobject::AUTO_WRITE
            ),
            mesh,
            dimensionedScalar(dimTime/dimDensity, 1)
        );
    }
 
    if (!runTime.restart() || !divergent())
    {
        correctUphiBCs(U_, phi_, true);
 
        fv::correctPhi
        (
            phi_,
            U,
            p_rgh,
            rAU,
            autoPtr<volScalarField>(),
            pressureReference(),
            pimple
        );
    }
}
 
 
// * * * * * * * * * * * * * * * * Destructor  * * * * * * * * * * * * * * * //
 
Foam::solvers::incompressibleDriftFlux::~incompressibleDriftFlux()
{}
 
 
// * * * * * * * * * * * * * * Member Functions  * * * * * * * * * * * * * * //
 
Foam::scalar Foam::solvers::incompressibleDriftFlux::maxDeltaT() const
{
    return fluidSolver::maxDeltaT();
}
 
 
void Foam::solvers::incompressibleDriftFlux::prePredictor()
{
    alphaPredictor();
 
    // Apply the diffusion term separately to allow implicit solution
    // and boundedness of the explicit advection
    {
        volScalarField nuEff(momentumTransport->nut());
        nuEff += packingDispersion->Dd();
 
        fvScalarMatrix alpha1Eqn
        (
            fvm::ddt(alpha1) - fvc::ddt(alpha1)
          - fvm::laplacian(nuEff, alpha1)
        );
 
        alpha1Eqn.solve(alpha1.name() + "Diffusion");
 
        alphaPhi1 += alpha1Eqn.flux();
 
        alpha2 = scalar(1) - alpha1;
        alphaPhi2 = phi - alphaPhi1;
 
        Info<< "Phase-1 volume fraction = "
            << alpha1.weightedAverage(mesh.Vsc()).value()
            << "  Min(" << alpha1.name() << ") = " << min(alpha1).value()
            << "  Max(" << alpha1.name() << ") = " << max(alpha1).value()
            << endl;
    }
 
    mixture.correct();
 
    const dimensionedScalar& rho1 = mixture.rho1();
    const dimensionedScalar& rho2 = mixture.rho2();
 
    // Calculate the mass-flux
    rhoPhi = alphaPhi1*rho1 + alphaPhi2*rho2;
 
    relativeVelocity->correct();
}
 
 
void Foam::solvers::incompressibleDriftFlux::momentumTransportPredictor()
{
    momentumTransport->predict();
}
 
 
void Foam::solvers::incompressibleDriftFlux::thermophysicalTransportPredictor()
{}
 
 
void Foam::solvers::incompressibleDriftFlux::pressureCorrector()
{
    incompressiblePressureCorrector(p);
}
 
 
void Foam::solvers::incompressibleDriftFlux::thermophysicalPredictor()
{}
 
 
void Foam::solvers::incompressibleDriftFlux::momentumTransportCorrector()
{
    momentumTransport->correct();
}
 
 
void Foam::solvers::incompressibleDriftFlux::thermophysicalTransportCorrector()
{}
 
 
// ************************************************************************* //