pEqn.H

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// Face volume fractions
PtrList<surfaceScalarField> alphafs(phases.size());
forAll(phases, phasei)
{
    phaseModel& phase = phases[phasei];
    const volScalarField& alpha = phase;
 
    alphafs.set(phasei, fvc::interpolate(alpha).ptr());
    alphafs[phasei].rename("pEqn" + alphafs[phasei].name());
}
 
// Diagonal coefficients
PtrList<volScalarField> rAUs(phases.size());
forAll(fluid.movingPhases(), movingPhasei)
{
    phaseModel& phase = fluid.movingPhases()[movingPhasei];
    const volScalarField& alpha = phase;
 
    rAUs.set
    (
        phase.index(),
        new volScalarField
        (
            IOobject::groupName("rAU", phase.name()),
            1.0
           /(
               UEqns[phase.index()].A()
             + byDt(max(phase.residualAlpha() - alpha, scalar(0))*phase.rho())
            )
        )
    );
}
fluid.fillFields("rAU", dimTime/dimDensity, rAUs);
 
// Phase diagonal coefficients
PtrList<surfaceScalarField> alpharAUfs(phases.size());
forAll(phases, phasei)
{
    phaseModel& phase = phases[phasei];
    const volScalarField& alpha = phase;
 
    alpharAUfs.set
    (
        phasei,
        (
            fvc::interpolate(max(alpha, phase.residualAlpha())*rAUs[phasei])
        ).ptr()
    );
}
 
// Explicit force fluxes
PtrList<surfaceScalarField> phiFs(fluid.phiFs(rAUs));
 
// --- Pressure corrector loop
while (pimple.correct())
{
    volScalarField rho("rho", fluid.rho());
 
    // Correct p_rgh for consistency with p and the updated densities
    p_rgh = p - rho*gh;
 
    // Correct fixed-flux BCs to be consistent with the velocity BCs
    forAll(fluid.movingPhases(), movingPhasei)
    {
        phaseModel& phase = fluid.movingPhases()[movingPhasei];
        MRF.correctBoundaryFlux(phase.U(), phase.phiRef());
    }
 
    // Combined buoyancy and force fluxes
    PtrList<surfaceScalarField> phigFs(phases.size());
    {
        const surfaceScalarField ghSnGradRho
        (
            "ghSnGradRho",
            ghf*fvc::snGrad(rho)*mesh.magSf()
        );
 
        forAll(phases, phasei)
        {
            phaseModel& phase = phases[phasei];
 
            phigFs.set
            (
                phasei,
                (
                    alpharAUfs[phasei]
                   *(
                       ghSnGradRho
                     - (fvc::interpolate(phase.rho() - rho))*(g & mesh.Sf())
                     - fluid.surfaceTension(phase)*mesh.magSf()
                    )
                ).ptr()
            );
 
            if (phiFs.set(phasei))
            {
                phigFs[phasei] += phiFs[phasei];
            }
        }
    }
 
    // Predicted velocities and fluxes for each phase
    PtrList<volVectorField> HbyAs(phases.size());
    PtrList<surfaceScalarField> phiHbyAs(phases.size());
    {
        // Correction force fluxes
        PtrList<surfaceScalarField> ddtCorrByAs(fluid.ddtCorrByAs(rAUs));
 
        forAll(fluid.movingPhases(), movingPhasei)
        {
            phaseModel& phase = fluid.movingPhases()[movingPhasei];
            const volScalarField& alpha = phase;
 
            HbyAs.set
            (
                phase.index(),
                new volVectorField
                (
                    IOobject::groupName("HbyA", phase.name()),
                    phase.U()
                )
            );
 
            HbyAs[phase.index()] =
                rAUs[phase.index()]
               *(
                    UEqns[phase.index()].H()
                  + byDt
                    (
                        max(phase.residualAlpha() - alpha, scalar(0))
                       *phase.rho()
                    )
                   *phase.U()().oldTime()
                );
 
            phiHbyAs.set
            (
                phase.index(),
                new surfaceScalarField
                (
                    IOobject::groupName("phiHbyA", phase.name()),
                    fvc::flux(HbyAs[phase.index()])
                  - phigFs[phase.index()]
                  - ddtCorrByAs[phase.index()]
                )
            );
        }
    }
    fluid.fillFields("HbyA", dimVelocity, HbyAs);
    fluid.fillFields("phiHbyA", dimForce/dimDensity/dimVelocity, phiHbyAs);
 
    // Add explicit drag forces and fluxes if not doing partial elimination
    if (!partialElimination)
    {
        PtrList<volVectorField> KdUByAs(fluid.KdUByAs(rAUs));
        PtrList<surfaceScalarField> phiKdPhis(fluid.phiKdPhis(rAUs));
 
        forAll(phases, phasei)
        {
            if (KdUByAs.set(phasei))
            {
                HbyAs[phasei] -= KdUByAs[phasei];
            }
            if (phiKdPhis.set(phasei))
            {
                phiHbyAs[phasei] -= phiKdPhis[phasei];
            }
        }
    }
 
    // Total predicted flux
    surfaceScalarField phiHbyA
    (
        IOobject
        (
            "phiHbyA",
            runTime.timeName(),
            mesh,
            IOobject::NO_READ,
            IOobject::AUTO_WRITE
        ),
        mesh,
        dimensionedScalar(dimVelocity*dimArea, Zero)
    );
 
    forAll(phases, phasei)
    {
        phiHbyA += alphafs[phasei]*phiHbyAs[phasei];
    }
 
    // Add explicit drag fluxes if doing partial elimination
    if (partialElimination)
    {
        PtrList<surfaceScalarField> phiKdPhis(fluid.phiKdPhis(rAUs));
 
        forAll(phases, phasei)
        {
            if (phiKdPhis.set(phasei))
            {
                phiHbyA -= alphafs[phasei]*phiKdPhis[phasei];
            }
        }
    }
 
    MRF.makeRelative(phiHbyA);
 
    // Construct pressure "diffusivity"
    surfaceScalarField rAUf
    (
        IOobject
        (
            "rAUf",
            runTime.timeName(),
            mesh
        ),
        mesh,
        dimensionedScalar("rAUf", dimensionSet(-1, 3, 1, 0, 0), 0)
    );
 
    forAll(phases, phasei)
    {
        rAUf += alphafs[phasei]*alpharAUfs[phasei];
    }
 
    rAUf = mag(rAUf);
 
    // Update the fixedFluxPressure BCs to ensure flux consistency
    {
        surfaceScalarField::Boundary phib(phi.boundaryField());
        phib = 0;
        forAll(phases, phasei)
        {
            phaseModel& phase = phases[phasei];
            phib +=
                alphafs[phasei].boundaryField()*phase.phi()().boundaryField();
        }
 
        setSnGrad<fixedFluxPressureFvPatchScalarField>
        (
            p_rgh.boundaryFieldRef(),
            (
                phiHbyA.boundaryField() - phib
            )/(mesh.magSf().boundaryField()*rAUf.boundaryField())
        );
    }
 
    // Compressible pressure equations
    PtrList<fvScalarMatrix> pEqnComps(phases.size());
    PtrList<volScalarField> dmdts(fluid.dmdts());
    forAll(phases, phasei)
    {
        phaseModel& phase = phases[phasei];
        const volScalarField& alpha = phase;
        volScalarField& rho = phase.thermoRef().rho();
 
        if (phase.compressible())
        {
            if (pimple.transonic())
            {
                surfaceScalarField phid
                (
                    IOobject::groupName("phid", phase.name()),
                    fvc::interpolate(phase.thermo().psi())*phase.phi()
                );
 
                pEqnComps.set
                (
                    phasei,
                    (
                        (
                            fvc::ddt(alpha, rho) + fvc::div(phase.alphaRhoPhi())
                          - fvc::Sp
                            (
                                fvc::ddt(alpha) + fvc::div(phase.alphaPhi()),
                                rho
                            )
                        )/rho
                      + correction
                        (
                            (alpha/rho)*
                            (
                                phase.thermo().psi()*fvm::ddt(p_rgh)
                              + fvm::div(phid, p_rgh)
                              - fvm::Sp(fvc::div(phid), p_rgh)
                            )
                        )
                    ).ptr()
                );
 
                pEqnComps[phasei].relax();
            }
            else
            {
                pEqnComps.set
                (
                    phasei,
                    (
                        (
                            fvc::ddt(alpha, rho) + fvc::div(phase.alphaRhoPhi())
                          - fvc::Sp
                            (
                                (fvc::ddt(alpha) + fvc::div(phase.alphaPhi())),
                                rho
                            )
                        )/rho
                      + (alpha*phase.thermo().psi()/rho)
                       *correction(fvm::ddt(p_rgh))
                    ).ptr()
                );
            }
        }
 
        // Add option sources
        if (fvOptions.appliesToField(rho.name()))
        {
            tmp<fvScalarMatrix> optEqn = fvOptions(alpha, rho);
            if (pEqnComps.set(phasei))
            {
                pEqnComps[phasei] -= (optEqn&rho)/rho;
            }
            else
            {
                pEqnComps.set
                (
                    phasei,
                    fvm::Su(- (optEqn&rho)/rho, p_rgh).ptr()
                );
            }
        }
 
        // Add mass transfer
        if (dmdts.set(phasei))
        {
            if (pEqnComps.set(phasei))
            {
                pEqnComps[phasei] -= dmdts[phasei]/rho;
            }
            else
            {
                pEqnComps.set
                (
                    phasei,
                    fvm::Su(- dmdts[phasei]/rho, p_rgh)
                );
            }
        }
    }
 
    // Cache p prior to solve for density update
    volScalarField p_rgh_0(p_rgh);
 
    // Iterate over the pressure equation to correct for non-orthogonality
    while (pimple.correctNonOrthogonal())
    {
        // Construct the transport part of the pressure equation
        fvScalarMatrix pEqnIncomp
        (
            fvc::div(phiHbyA)
          - fvm::laplacian(rAUf, p_rgh)
        );
 
        {
            fvScalarMatrix pEqn(pEqnIncomp);
 
            forAll(phases, phasei)
            {
                if (pEqnComps.set(phasei))
                {
                    pEqn += pEqnComps[phasei];
                }
            }
 
            pEqn.solve(p_rgh.select(pimple.finalInnerIter()));
        }
 
        // Correct fluxes and velocities on last non-orthogonal iteration
        if (pimple.finalNonOrthogonalIter())
        {
            phi = phiHbyA + pEqnIncomp.flux();
 
            surfaceScalarField mSfGradp("mSfGradp", pEqnIncomp.flux()/rAUf);
 
            forAll(fluid.movingPhases(), movingPhasei)
            {
                phaseModel& phase = fluid.movingPhases()[movingPhasei];
 
                phase.phiRef() =
                    phiHbyAs[phase.index()]
                  + alpharAUfs[phase.index()]*mSfGradp;
 
                // Set the phase dilatation rates
                if (pEqnComps.set(phase.index()))
                {
                    phase.divU(-pEqnComps[phase.index()] & p_rgh);
                }
            }
 
            // Optionally relax pressure for velocity correction
            p_rgh.relax();
 
            mSfGradp = pEqnIncomp.flux()/rAUf;
 
            forAll(fluid.movingPhases(), movingPhasei)
            {
                phaseModel& phase = fluid.movingPhases()[movingPhasei];
 
                phase.URef() =
                    HbyAs[phase.index()]
                  + fvc::reconstruct
                    (
                        alpharAUfs[phase.index()]*mSfGradp
                      - phigFs[phase.index()]
                    );
            }
 
            if (partialElimination)
            {
                fluid.partialElimination(rAUs);
            }
 
            forAll(fluid.movingPhases(), movingPhasei)
            {
                phaseModel& phase = fluid.movingPhases()[movingPhasei];
 
                phase.URef().correctBoundaryConditions();
                fvOptions.correct(phase.URef());
            }
        }
    }
 
    // Update and limit the static pressure
    p = max(p_rgh + rho*gh, pMin);
 
    // Limit p_rgh
    p_rgh = p - rho*gh;
 
    // Update densities from change in p_rgh
    forAll(phases, phasei)
    {
        phaseModel& phase = phases[phasei];
        phase.thermoRef().rho() += phase.thermo().psi()*(p_rgh - p_rgh_0);
    }
 
    // Correct p_rgh for consistency with p and the updated densities
    rho = fluid.rho();
    p_rgh = p - rho*gh;
    p_rgh.correctBoundaryConditions();
}