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/*---------------------------------------------------------------------------*\
========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration |
\\ / A nd | Copyright (C) 2011-2015 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/>.
Class
Foam::heatTransferModel
Description
SourceFiles
heatTransferModel.C
newHeatTransferModel.C
\*---------------------------------------------------------------------------*/
#ifndef heatTransferModel_H
#define heatTransferModel_H
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
#include "dictionary.H"
#include "phaseModel.H"
#include "runTimeSelectionTables.H"
namespace Foam
{
/*---------------------------------------------------------------------------*\
Class heatTransferModel Declaration
\*---------------------------------------------------------------------------*/
class heatTransferModel
{
protected:
// Protected data
const dictionary& interfaceDict_;
const volScalarField& alpha1_;
const phaseModel& phase1_;
const phaseModel& phase2_;
public:
//- Runtime type information
TypeName("heatTransferModel");
// Declare runtime construction
declareRunTimeSelectionTable
(
autoPtr,
heatTransferModel,
dictionary,
(
const dictionary& interfaceDict,
const volScalarField& alpha1,
const phaseModel& phase1,
const phaseModel& phase2
),
(interfaceDict, alpha1, phase1, phase2)
);
// Constructors
heatTransferModel
(
const dictionary& interfaceDict,
const volScalarField& alpha1,
const phaseModel& phase1,
const phaseModel& phase2
);
//- Destructor
virtual ~heatTransferModel();
// Selectors
static autoPtr<heatTransferModel> New
(
const dictionary& interfaceDict,
const volScalarField& alpha1,
const phaseModel& phase1,
const phaseModel& phase2
);
// Member Functions
//- The heat-transfer function K used in the enthalpy eq.
// ddt(alpha1*rho1*ha) + ... = ... alpha1*alpha2*K*(Ta - Tb)
// ddt(alpha2*rho2*hb) + ... = ... alpha1*alpha2*K*(Tb - Ta)
// ********************************** NB! *****************************
// for numerical reasons alpha1 and alpha2 has been
// extracted from the heat-transfer function K,
// so you MUST divide K by alpha1*alpha2 when implementing the
// heat-transfer function
// ********************************** NB! *****************************
virtual tmp<volScalarField> K(const volScalarField& Ur) const = 0;
};
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
} // End namespace Foam
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
#endif
// ************************************************************************* //
|
