TwoResistanceHeatTransferPhaseSystem.C

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    Copyright (C) 2015-2019 OpenFOAM Foundation
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License
    This file is part of OpenFOAM.
 
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    for more details.
 
    You should have received a copy of the GNU General Public License
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#include "TwoResistanceHeatTransferPhaseSystem.H"
 
#include "BlendedInterfacialModel.H"
#include "heatTransferModel.H"
 
#include "HashPtrTable.H"
 
#include "fvcDiv.H"
#include "fvmSup.H"
#include "fvMatrix.H"
#include "zeroGradientFvPatchFields.H"
 
// * * * * * * * * * * * * * * * * Constructors  * * * * * * * * * * * * * * //
 
template<class BasePhaseSystem>
Foam::TwoResistanceHeatTransferPhaseSystem<BasePhaseSystem>::
TwoResistanceHeatTransferPhaseSystem
(
    const fvMesh& mesh
)
:
    BasePhaseSystem(mesh)
{
    this->generatePairsAndSubModels
    (
        "heatTransfer",
        heatTransferModels_,
        false
    );
 
    // Check that models have been specified on both sides of the interfaces
    forAllConstIter
    (
        heatTransferModelTable,
        heatTransferModels_,
        heatTransferModelIter
    )
    {
        const phasePair& pair = this->phasePairs_[heatTransferModelIter.key()];
 
        if (!heatTransferModels_[pair].first())
        {
            FatalErrorInFunction
                << "A heat transfer model for the " << pair.phase1().name()
                << " side of the " << pair << " pair is not specified"
                << exit(FatalError);
        }
        if (!heatTransferModels_[pair].second())
        {
            FatalErrorInFunction
                << "A heat transfer model for the " << pair.phase2().name()
                << " side of the " << pair << " pair is not specified"
                << exit(FatalError);
        }
    }
 
    // Calculate initial Tf-s as if there is no mass transfer
    forAllConstIter
    (
        heatTransferModelTable,
        heatTransferModels_,
        heatTransferModelIter
    )
    {
        const phasePair& pair = this->phasePairs_[heatTransferModelIter.key()];
 
        const phaseModel& phase1 = pair.phase1();
        const phaseModel& phase2 = pair.phase2();
 
        const volScalarField& T1(phase1.thermo().T());
        const volScalarField& T2(phase2.thermo().T());
 
        volScalarField H1(heatTransferModels_[pair].first()->K());
        volScalarField H2(heatTransferModels_[pair].second()->K());
        dimensionedScalar HSmall("small", heatTransferModel::dimK, SMALL);
 
        Tf_.set
        (
            pair,
            new volScalarField
            (
                IOobject
                (
                    IOobject::groupName("Tf", pair.name()),
                    this->mesh().time().timeName(),
                    this->mesh(),
                    IOobject::NO_READ,
                    IOobject::AUTO_WRITE
                ),
                (H1*T1 + H2*T2)/max(H1 + H2, HSmall)
            )
        );
    }
}
 
 
// * * * * * * * * * * * * * * * * Destructor  * * * * * * * * * * * * * * * //
 
template<class BasePhaseSystem>
Foam::TwoResistanceHeatTransferPhaseSystem<BasePhaseSystem>::
~TwoResistanceHeatTransferPhaseSystem()
{}
 
 
// * * * * * * * * * * * * * * Member Functions  * * * * * * * * * * * * * * //
 
template<class BasePhaseSystem>
Foam::autoPtr<Foam::phaseSystem::heatTransferTable>
Foam::TwoResistanceHeatTransferPhaseSystem<BasePhaseSystem>::
heatTransfer() const
{
    autoPtr<phaseSystem::heatTransferTable> eqnsPtr
    (
        new phaseSystem::heatTransferTable()
    );
 
    phaseSystem::heatTransferTable& eqns = eqnsPtr();
 
    forAll(this->phaseModels_, phasei)
    {
        const phaseModel& phase = this->phaseModels_[phasei];
 
        eqns.set
        (
            phase.name(),
            new fvScalarMatrix(phase.thermo().he(), dimEnergy/dimTime)
        );
    }
 
    // Heat transfer with the interface
    forAllConstIter
    (
        heatTransferModelTable,
        heatTransferModels_,
        heatTransferModelIter
    )
    {
        const phasePair& pair
        (
            this->phasePairs_[heatTransferModelIter.key()]
        );
 
        const volScalarField& Tf(*Tf_[pair]);
 
        const Pair<tmp<volScalarField>> Ks
        (
            heatTransferModelIter().first()->K(),
            heatTransferModelIter().second()->K()
        );
 
        forAllConstIter(phasePair, pair, iter)
        {
            const phaseModel& phase = iter();
 
            const volScalarField& he(phase.thermo().he());
            const volScalarField Cpv(phase.thermo().Cpv());
            const volScalarField& K(Ks[iter.index()]);
 
            *eqns[phase.name()] +=
                K*(Tf - phase.thermo().T())
              + K/Cpv*he - fvm::Sp(K/Cpv, he);
        }
    }
 
    // Source term due to mass transfer
    forAllConstIter
    (
        phaseSystem::phasePairTable,
        this->phasePairs_,
        phasePairIter
    )
    {
        const phasePair& pair(phasePairIter());
 
        if (pair.ordered())
        {
            continue;
        }
 
        const phaseModel& phase1 = pair.phase1();
        const phaseModel& phase2 = pair.phase2();
 
        const volScalarField& he1(phase1.thermo().he());
        const volScalarField& he2(phase2.thermo().he());
 
        const volScalarField K1(phase1.K());
        const volScalarField K2(phase2.K());
 
        const volScalarField dmdt(this->dmdt(pair));
        const volScalarField dmdt21(posPart(dmdt));
        const volScalarField dmdt12(negPart(dmdt));
 
        *eqns[phase1.name()] += - fvm::Sp(dmdt21, he1) + dmdt21*(K2 - K1);
 
        *eqns[phase2.name()] -= - fvm::Sp(dmdt12, he2) + dmdt12*(K1 - K2);
 
        if (this->heatTransferModels_.found(phasePairIter.key()))
        {
            const volScalarField& Tf(*Tf_[pair]);
 
            *eqns[phase1.name()] +=
                dmdt21*phase1.thermo().he(phase1.thermo().p(), Tf);
 
            *eqns[phase2.name()] -=
                dmdt12*phase2.thermo().he(phase2.thermo().p(), Tf);
        }
        else
        {
            *eqns[phase1.name()] += dmdt21*he2;
 
            *eqns[phase2.name()] -= dmdt12*he1;
        }
    }
 
    return eqnsPtr;
}
 
 
template<class BasePhaseSystem>
void Foam::TwoResistanceHeatTransferPhaseSystem<BasePhaseSystem>::
correctEnergyTransport()
{
    BasePhaseSystem::correctEnergyTransport();
 
    correctInterfaceThermo();
}
 
 
template<class BasePhaseSystem>
void Foam::TwoResistanceHeatTransferPhaseSystem<BasePhaseSystem>::
correctInterfaceThermo()
{
    forAllConstIter
    (
        heatTransferModelTable,
        heatTransferModels_,
        heatTransferModelIter
    )
    {
        const phasePair& pair
        (
            this->phasePairs_[heatTransferModelIter.key()]
        );
 
        const phaseModel& phase1 = pair.phase1();
        const phaseModel& phase2 = pair.phase2();
 
        const volScalarField& p(phase1.thermo().p());
 
        const volScalarField& T1(phase1.thermo().T());
        const volScalarField& T2(phase2.thermo().T());
 
        volScalarField& Tf(*this->Tf_[pair]);
 
        const volScalarField L
        (
            phase1.thermo().he(p, Tf) - phase2.thermo().he(p, Tf)
        );
 
        const volScalarField dmdt(this->dmdt(pair));
 
        volScalarField H1
        (
            this->heatTransferModels_[pair].first()->K()
        );
 
        volScalarField H2
        (
            this->heatTransferModels_[pair].second()->K()
        );
 
        // Limit the H[12] to avoid /0
        H1.clamp_min(SMALL);
        H2.clamp_min(SMALL);
 
        Tf = (H1*T1 + H2*T2 + dmdt*L)/(H1 + H2);
 
        Info<< "Tf." << pair.name()
            << ": min = " << min(Tf.primitiveField())
            << ", mean = " << average(Tf.primitiveField())
            << ", max = " << max(Tf.primitiveField())
            << endl;
    }
}
 
 
template<class BasePhaseSystem>
bool Foam::TwoResistanceHeatTransferPhaseSystem<BasePhaseSystem>::read()
{
    if (BasePhaseSystem::read())
    {
        bool readOK = true;
 
        // Models ...
 
        return readOK;
    }
    else
    {
        return false;
    }
}
 
 
// ************************************************************************* //