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reactingTwoPhaseEulerFoam: Corrected handling of heat-transfer caused by mass-transfer

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This commit is contained in:
Henry Weller
2015-07-02 22:51:06 +01:00
parent be16ebf24f
commit 68ea75a37c
7 changed files with 55 additions and 16 deletions
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32
applications/solvers/multiphase/reactingTwoPhaseEulerFoam/phaseSystems/PhaseSystems/HeatAndMassTransferPhaseSystem/HeatAndMassTransferPhaseSystem.C
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@ -288,6 +288,38 @@ Foam::HeatAndMassTransferPhaseSystem<BasePhaseSystem>::heatTransfer() const
}
}
// Source term due to mass trasfer
forAllConstIter
(
phaseSystem::phasePairTable,
this->phasePairs_,
phasePairIter
)
{
const phasePair& pair(phasePairIter());
if (pair.ordered())
{
continue;
}
const volScalarField& he1(pair.phase1().thermo().he());
const volScalarField& he2(pair.phase2().thermo().he());
const volScalarField& K1(pair.phase1().K());
const volScalarField& K2(pair.phase2().K());
const volScalarField dmdt(this->dmdt(pair));
const volScalarField dmdt12(dmdt*pos(dmdt));
const volScalarField dmdt21(dmdt*neg(dmdt));
*eqns[pair.phase1().name()] +=
fvm::Sp(dmdt21, he1) + dmdt21*K1 - dmdt21*(he2 + K2);
*eqns[pair.phase2().name()] +=
dmdt12*(he1 + K1) - fvm::Sp(dmdt12, he2) - dmdt12*K2;
}
return eqnsPtr;
}

8
applications/solvers/multiphase/reactingTwoPhaseEulerFoam/phaseSystems/phaseModel/AnisothermalPhaseModel/AnisothermalPhaseModel.C
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@ -154,4 +154,12 @@ Foam::AnisothermalPhaseModel<BasePhaseModel>::divU(const volScalarField& divU)
}
template<class BasePhaseModel>
const Foam::volScalarField&
Foam::AnisothermalPhaseModel<BasePhaseModel>::K() const
{
return K_;
}
// ************************************************************************* //

7
applications/solvers/multiphase/reactingTwoPhaseEulerFoam/phaseSystems/phaseModel/AnisothermalPhaseModel/AnisothermalPhaseModel.H
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@ -89,11 +89,14 @@ public:
//- Return true if the phase is compressible otherwise false
virtual bool compressible() const;
//- Phase dilatation rate (d(alpha)/dt + div(alpha*phi))
//- Return the phase dilatation rate (d(alpha)/dt + div(alpha*phi))
virtual const volScalarField& divU() const;
//- Set phase dilatation rate (d(alpha)/dt + div(alpha*phi))
//- Set the phase dilatation rate (d(alpha)/dt + div(alpha*phi))
virtual void divU(const volScalarField& divU);
//- Return the phase kinetic energy
virtual const volScalarField& K() const;
};

8
applications/solvers/multiphase/reactingTwoPhaseEulerFoam/phaseSystems/phaseModel/MovingPhaseModel/MovingPhaseModel.C
View File

@ -314,14 +314,6 @@ Foam::MovingPhaseModel<BasePhaseModel>::continuityError() const
}
template<class BasePhaseModel>
Foam::volScalarField&
Foam::MovingPhaseModel<BasePhaseModel>::continuityError()
{
return continuityError_;
}
template<class BasePhaseModel>
Foam::tmp<Foam::surfaceScalarField>
Foam::MovingPhaseModel<BasePhaseModel>::phi() const

3
applications/solvers/multiphase/reactingTwoPhaseEulerFoam/phaseSystems/phaseModel/MovingPhaseModel/MovingPhaseModel.H
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@ -152,9 +152,6 @@ public:
//- Constant access the continuity error
virtual tmp<volScalarField> continuityError() const;
//- Access the continuity error
virtual volScalarField& continuityError();
//- Constant access the volumetric flux
virtual tmp<surfaceScalarField> phi() const;

7
applications/solvers/multiphase/reactingTwoPhaseEulerFoam/phaseSystems/phaseModel/phaseModel/phaseModel.C
View File

@ -155,6 +155,13 @@ void Foam::phaseModel::divU(const volScalarField& divU)
}
const Foam::volScalarField& Foam::phaseModel::K() const
{
notImplemented("Foam::phaseModel::K()");
return volScalarField::null();
}
const Foam::surfaceScalarField& Foam::phaseModel::DbyA() const
{
return surfaceScalarField::null();

6
applications/solvers/multiphase/reactingTwoPhaseEulerFoam/phaseSystems/phaseModel/phaseModel/phaseModel.H
View File

@ -175,6 +175,9 @@ public:
//- Set the phase dilatation rate (d(alpha)/dt + div(alpha*phi))
virtual void divU(const volScalarField& divU);
//- Return the phase kinetic energy
virtual const volScalarField& K() const;
// Implicit phase pressure and dispersion support
@ -218,9 +221,6 @@ public:
//- Constant access the continuity error
virtual tmp<volScalarField> continuityError() const = 0;
//- Access the continuity error
virtual volScalarField& continuityError() = 0;
//- Constant access the volumetric flux
virtual tmp<surfaceScalarField> phi() const = 0;