openfoam/applications/solvers/multiphase/compressibleInterFoam/VoFphaseCompressibleTurbulenceModels/compressibleInterPhaseTransportModel.H

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/*---------------------------------------------------------------------------*\
========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration |
\\ / A nd | Copyright (C) 2017-2018 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
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Class
Foam::compressibleInterPhaseTransportModel
Description
Transport model selection class for the compressibleInterFoam family of
solvers.
By default the standard mixture transport modelling approach is used in
which a single momentum stress model (laminar, non-Newtonian, LES or RAS) is
constructed for the mixture. However if the \c simulationType in
constant/turbulenceProperties is set to \c twoPhaseTransport the alternative
Euler-Euler two-phase transport modelling approach is used in which separate
stress models (laminar, non-Newtonian, LES or RAS) are instantiated for each
of the two phases allowing for different modeling for the phases.
SourceFiles
compressibleInterPhaseTransportModel.C
\*---------------------------------------------------------------------------*/
#ifndef compressibleInterPhaseTransportModel_H
#define compressibleInterPhaseTransportModel_H
#include "twoPhaseMixture.H"
#include "twoPhaseMixtureThermo.H"
#include "turbulentFluidThermoModel.H"
#include "VoFphaseCompressibleTurbulenceModel.H"
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
namespace Foam
{
/*---------------------------------------------------------------------------*\
Class compressibleInterPhaseTransportModel Declaration
\*---------------------------------------------------------------------------*/
class compressibleInterPhaseTransportModel
{
// Private data
//- Switch to select two-phase or mixture transport modelling
Switch twoPhaseTransport_;
//- Two-phase mixture
const twoPhaseMixtureThermo& mixture_;
//- Mixture volumetric flux
const surfaceScalarField& phi_;
//- Phase volumetric flux
const surfaceScalarField& alphaPhi10_;
//- Phase-1 mass-flux (constructed for two-phase transport)
tmp<surfaceScalarField> alphaRhoPhi1_;
//- Phase-2 mass-flux (constructed for two-phase transport)
tmp<surfaceScalarField> alphaRhoPhi2_;
//- Mixture transport model (constructed for mixture transport)
autoPtr<compressible::turbulenceModel> turbulence_;
//- Phase-1 transport model (constructed for two-phase transport)
autoPtr
<
ThermalDiffusivity<PhaseCompressibleTurbulenceModel<fluidThermo>>
> turbulence1_;
//- Phase-2 transport model (constructed for two-phase transport)
autoPtr
<
ThermalDiffusivity<PhaseCompressibleTurbulenceModel<fluidThermo>>
> turbulence2_;
// Private Member Functions
//- No copy construct
compressibleInterPhaseTransportModel
(
const compressibleInterPhaseTransportModel&
) = delete;
//- No copy assignment
void operator=(const compressibleInterPhaseTransportModel&) = delete;
public:
// Constructors
//- Construct from components
compressibleInterPhaseTransportModel
(
const volScalarField& rho,
const volVectorField& U,
const surfaceScalarField& phi,
const surfaceScalarField& rhoPhi,
const surfaceScalarField& alphaPhi10,
const twoPhaseMixtureThermo& mixture
);
// Member Functions
//- Return the effective temperature transport coefficient
tmp<volScalarField> alphaEff() const;
//- Return the effective momentum stress divergence
tmp<fvVectorMatrix> divDevRhoReff(volVectorField& U) const;
//- Correct the phase mass-fluxes
// (required for the two-phase transport option)
void correctPhasePhi();
//- Correct the phase or mixture transport models
void correct();
};
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
} // End namespace Foam
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
#endif
// ************************************************************************* //