Files
openfoam/applications/solvers/multiphase/reactingEulerFoam/phaseSystems/PhaseSystems/InterfaceCompositionPhaseChangePhaseSystem/InterfaceCompositionPhaseChangePhaseSystem.C
Mark Olesen 2f86cdc712 STYLE: more consistent use of dimensioned Zero
- when constructing dimensioned fields that are to be zero-initialized,
  it is preferrable to use a form such as

      dimensionedScalar(dims, Zero)
      dimensionedVector(dims, Zero)

  rather than

      dimensionedScalar("0", dims, 0)
      dimensionedVector("zero", dims, vector::zero)

  This reduces clutter and also avoids any suggestion that the name of
  the dimensioned quantity has any influence on the field's name.

  An even shorter version is possible. Eg,

      dimensionedScalar(dims)

  but reduces the clarity of meaning.

- NB: UniformDimensionedField is an exception to these style changes
  since it does use the name of the dimensioned type (instead of the
  regIOobject).
2018-03-16 10:24:03 +01:00

318 lines
9.1 KiB
C

/*---------------------------------------------------------------------------*\
========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration |
\\ / A nd | Copyright (C) 2015-2016 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/>.
\*---------------------------------------------------------------------------*/
#include "InterfaceCompositionPhaseChangePhaseSystem.H"
#include "interfaceCompositionModel.H"
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
template<class BasePhaseSystem>
Foam::InterfaceCompositionPhaseChangePhaseSystem<BasePhaseSystem>::
InterfaceCompositionPhaseChangePhaseSystem
(
const fvMesh& mesh
)
:
HeatAndMassTransferPhaseSystem<BasePhaseSystem>(mesh)
{
this->generatePairsAndSubModels
(
"interfaceComposition",
interfaceCompositionModels_
);
}
// * * * * * * * * * * * * * * * * Destructor * * * * * * * * * * * * * * * //
template<class BasePhaseSystem>
Foam::InterfaceCompositionPhaseChangePhaseSystem<BasePhaseSystem>::
~InterfaceCompositionPhaseChangePhaseSystem()
{}
// * * * * * * * * * * * * * * Member Functions * * * * * * * * * * * * * * //
template<class BasePhaseSystem>
Foam::autoPtr<Foam::phaseSystem::massTransferTable>
Foam::InterfaceCompositionPhaseChangePhaseSystem<BasePhaseSystem>::
massTransfer() const
{
// Create a mass transfer matrix for each species of each phase
autoPtr<phaseSystem::massTransferTable> eqnsPtr
(
new phaseSystem::massTransferTable()
);
phaseSystem::massTransferTable& eqns = eqnsPtr();
forAll(this->phaseModels_, phasei)
{
const phaseModel& phase = this->phaseModels_[phasei];
const PtrList<volScalarField>& Yi = phase.Y();
forAll(Yi, i)
{
eqns.insert
(
Yi[i].name(),
new fvScalarMatrix(Yi[i], dimMass/dimTime)
);
}
}
// Reset the interfacial mass flow rates
forAllConstIters(this->phasePairs_, phasePairIter)
{
const phasePair& pair = *(phasePairIter.object());
if (pair.ordered())
{
continue;
}
*this->dmdt_[pair] =
*this->dmdtExplicit_[pair];
*this->dmdtExplicit_[pair] =
dimensionedScalar(dimDensity/dimTime, Zero);
}
// Sum up the contribution from each interface composition model
forAllConstIters
(
interfaceCompositionModels_,
interfaceCompositionModelIter
)
{
const phasePair& pair =
*(this->phasePairs_[interfaceCompositionModelIter.key()]);
const interfaceCompositionModel& compositionModel =
*(interfaceCompositionModelIter.object());
const phaseModel& phase = pair.phase1();
const phaseModel& otherPhase = pair.phase2();
const phasePairKey key(phase.name(), otherPhase.name());
const volScalarField& Tf(*this->Tf_[key]);
volScalarField& dmdtExplicit(*this->dmdtExplicit_[key]);
volScalarField& dmdt(*this->dmdt_[key]);
scalar dmdtSign(Pair<word>::compare(this->dmdt_.find(key).key(), key));
const volScalarField K
(
this->massTransferModels_[key][phase.name()]->K()
);
forAllConstIter
(
hashedWordList,
compositionModel.species(),
memberIter
)
{
const word& member = *memberIter;
const word name
(
IOobject::groupName(member, phase.name())
);
const word otherName
(
IOobject::groupName(member, otherPhase.name())
);
const volScalarField KD
(
K*compositionModel.D(member)
);
const volScalarField Yf
(
compositionModel.Yf(member, Tf)
);
// Implicit transport through the phase
*eqns[name] +=
phase.rho()*KD*Yf
- fvm::Sp(phase.rho()*KD, eqns[name]->psi());
// Sum the mass transfer rate
dmdtExplicit += dmdtSign*phase.rho()*KD*Yf;
dmdt -= dmdtSign*phase.rho()*KD*eqns[name]->psi();
// Explicit transport out of the other phase
if (eqns.found(otherName))
{
*eqns[otherName] -=
otherPhase.rho()*KD*compositionModel.dY(member, Tf);
}
}
}
return eqnsPtr;
}
template<class BasePhaseSystem>
void Foam::InterfaceCompositionPhaseChangePhaseSystem<BasePhaseSystem>::
correctThermo()
{
BasePhaseSystem::correctThermo();
// This loop solves for the interface temperatures, Tf, and updates the
// interface composition models.
//
// The rate of heat transfer to the interface must equal the latent heat
// consumed at the interface, i.e.:
//
// H1*(T1 - Tf) + H2*(T2 - Tf) == mDotL
// == K*rho*(Yfi - Yi)*Li
//
// Yfi is likely to be a strong non-linear (typically exponential) function
// of Tf, so the solution for the temperature is newton-accelerated
forAllConstIters(this->phasePairs_, phasePairIter)
{
const phasePair& pair = *(phasePairIter.object());
if (pair.ordered())
{
continue;
}
const phasePairKey key12(pair.first(), pair.second(), true);
const phasePairKey key21(pair.second(), pair.first(), true);
volScalarField H1(this->heatTransferModels_[pair][pair.first()]->K());
volScalarField H2(this->heatTransferModels_[pair][pair.second()]->K());
dimensionedScalar HSmall("small", heatTransferModel::dimK, SMALL);
volScalarField mDotL
(
IOobject
(
"mDotL",
this->mesh().time().timeName(),
this->mesh()
),
this->mesh(),
dimensionedScalar(dimEnergy/dimVolume/dimTime, Zero)
);
volScalarField mDotLPrime
(
IOobject
(
"mDotLPrime",
this->mesh().time().timeName(),
this->mesh()
),
this->mesh(),
dimensionedScalar(mDotL.dimensions()/dimTemperature, Zero)
);
volScalarField& Tf = *this->Tf_[pair];
// Add latent heats from forward and backward models
if (this->interfaceCompositionModels_.found(key12))
{
this->interfaceCompositionModels_[key12]->addMDotL
(
this->massTransferModels_[pair][pair.first()]->K(),
Tf,
mDotL,
mDotLPrime
);
}
if (this->interfaceCompositionModels_.found(key21))
{
this->interfaceCompositionModels_[key21]->addMDotL
(
this->massTransferModels_[pair][pair.second()]->K(),
Tf,
mDotL,
mDotLPrime
);
}
// Update the interface temperature by applying one step of newton's
// method to the interface relation
Tf -=
(
H1*(Tf - pair.phase1().thermo().T())
+ H2*(Tf - pair.phase2().thermo().T())
+ mDotL
)
/(
max(H1 + H2 + mDotLPrime, HSmall)
);
Tf.correctBoundaryConditions();
Info<< "Tf." << pair.name()
<< ": min = " << min(Tf.primitiveField())
<< ", mean = " << average(Tf.primitiveField())
<< ", max = " << max(Tf.primitiveField())
<< endl;
// Update the interface compositions
if (this->interfaceCompositionModels_.found(key12))
{
this->interfaceCompositionModels_[key12]->update(Tf);
}
if (this->interfaceCompositionModels_.found(key21))
{
this->interfaceCompositionModels_[key21]->update(Tf);
}
}
}
template<class BasePhaseSystem>
bool Foam::InterfaceCompositionPhaseChangePhaseSystem<BasePhaseSystem>::read()
{
if (BasePhaseSystem::read())
{
bool readOK = true;
// Models ...
return readOK;
}
else
{
return false;
}
}
// ************************************************************************* //