242 lines
6.8 KiB
C++
242 lines
6.8 KiB
C++
/*---------------------------------------------------------------------------*\
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========= |
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\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
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\\ / O peration |
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\\ / A nd | Copyright (C) 2013-2016 OpenFOAM Foundation
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\\/ M anipulation |
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-------------------------------------------------------------------------------
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License
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This file is part of OpenFOAM.
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OpenFOAM is free software: you can redistribute it and/or modify it
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under the terms of the GNU General Public License as published by
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the Free Software Foundation, either version 3 of the License, or
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(at your option) any later version.
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OpenFOAM is distributed in the hope that it will be useful, but WITHOUT
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ANY WARRANTY; without even the implied warranty of MERCHANTABILITY or
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FITNESS FOR A PARTICULAR PURPOSE. See the GNU General Public License
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for more details.
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You should have received a copy of the GNU General Public License
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along with OpenFOAM. If not, see <http://www.gnu.org/licenses/>.
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Class
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Foam::twoPhaseSystem
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Description
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SourceFiles
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twoPhaseSystem.C
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\*---------------------------------------------------------------------------*/
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#ifndef twoPhaseSystem_H
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#define twoPhaseSystem_H
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#include "IOdictionary.H"
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#include "phaseModel.H"
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#include "phasePair.H"
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#include "orderedPhasePair.H"
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#include "volFields.H"
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#include "surfaceFields.H"
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#include "dragModel.H"
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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namespace Foam
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{
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class virtualMassModel;
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class heatTransferModel;
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class liftModel;
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class wallLubricationModel;
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class turbulentDispersionModel;
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class blendingMethod;
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template<class modelType> class BlendedInterfacialModel;
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/*---------------------------------------------------------------------------*\
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Class twoPhaseSystem Declaration
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\*---------------------------------------------------------------------------*/
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class twoPhaseSystem
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:
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public IOdictionary
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{
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// Private data
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//- Reference to the mesh
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const fvMesh& mesh_;
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//- Phase model 1
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phaseModel phase1_;
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//- Phase model 2
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phaseModel phase2_;
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//- Total volumetric flux
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surfaceScalarField phi_;
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//- Dilatation term
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volScalarField dgdt_;
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//- Optional dispersion diffusivity
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tmp<surfaceScalarField> pPrimeByA_;
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//- Unordered phase pair
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autoPtr<phasePair> pair_;
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//- Phase pair for phase 1 dispersed in phase 2
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autoPtr<orderedPhasePair> pair1In2_;
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//- Phase pair for phase 2 dispersed in phase 1
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autoPtr<orderedPhasePair> pair2In1_;
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//- Blending methods
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HashTable<autoPtr<blendingMethod>> blendingMethods_;
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//- Drag model
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autoPtr<BlendedInterfacialModel<dragModel>> drag_;
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//- Virtual mass model
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autoPtr<BlendedInterfacialModel<virtualMassModel>> virtualMass_;
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//- Heat transfer model
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autoPtr<BlendedInterfacialModel<heatTransferModel>> heatTransfer_;
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//- Lift model
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autoPtr<BlendedInterfacialModel<liftModel>> lift_;
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//- Wall lubrication model
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autoPtr<BlendedInterfacialModel<wallLubricationModel>>
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wallLubrication_;
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//- Wall lubrication model
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autoPtr<BlendedInterfacialModel<turbulentDispersionModel>>
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turbulentDispersion_;
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// Private member functions
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//- Return the mixture flux
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tmp<surfaceScalarField> calcPhi() const;
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public:
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// Constructors
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//- Construct from fvMesh
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twoPhaseSystem(const fvMesh&, const dimensionedVector& g);
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//- Destructor
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virtual ~twoPhaseSystem();
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// Member Functions
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//- Return the mixture density
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tmp<volScalarField> rho() const;
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//- Return the mixture velocity
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tmp<volVectorField> U() const;
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//- Return the drag coefficient
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tmp<volScalarField> Kd() const;
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//- Return the face drag coefficient
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tmp<surfaceScalarField> Kdf() const;
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//- Return the virtual mass coefficient
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tmp<volScalarField> Vm() const;
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//- Return the face virtual mass coefficient
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tmp<surfaceScalarField> Vmf() const;
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//- Return the heat transfer coefficient
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tmp<volScalarField> Kh() const;
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//- Return the combined force (lift + wall-lubrication)
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tmp<volVectorField> F() const;
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//- Return the combined face-force (lift + wall-lubrication)
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tmp<surfaceScalarField> Ff() const;
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//- Return the turbulent diffusivity
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// Multiplies the phase-fraction gradient
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tmp<volScalarField> D() const;
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//- Solve for the two-phase-fractions
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void solve();
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//- Correct two-phase properties other than turbulence
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void correct();
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//- Correct two-phase turbulence
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void correctTurbulence();
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//- Read base phaseProperties dictionary
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bool read();
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// Access
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//- Return the drag model for the given phase
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const dragModel& drag(const phaseModel& phase) const;
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//- Return the virtual mass model for the given phase
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const virtualMassModel& virtualMass(const phaseModel& phase) const;
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//- Return the surface tension coefficient
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const dimensionedScalar& sigma() const;
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//- Return the mesh
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inline const fvMesh& mesh() const;
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//- Return phase model 1
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inline const phaseModel& phase1() const;
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//- Return non-const access to phase model 1
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inline phaseModel& phase1();
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//- Return phase model 2
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inline const phaseModel& phase2() const;
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//- Return non-const access to phase model 2
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inline phaseModel& phase2();
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//- Return the phase not given as an argument
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inline const phaseModel& otherPhase(const phaseModel& phase) const;
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//- Return the mixture flux
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inline const surfaceScalarField& phi() const;
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//- Return non-const access to the mixture flux
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inline surfaceScalarField& phi();
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//- Return the dilatation term
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inline const volScalarField& dgdt() const;
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//- Return non-const access to the dilatation parameter
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inline volScalarField& dgdt();
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//- Return non-const access to the dispersion diffusivity
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inline tmp<surfaceScalarField>& pPrimeByA();
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};
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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} // End namespace Foam
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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#include "twoPhaseSystemI.H"
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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#endif
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// ************************************************************************* //
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