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========= |
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\\ / O peration |
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Class
Foam::meltingEvaporationModels::diffusionGasEvaporation
Description
Gas diffusion based evaporation/condensation mass transfer model.
THE evaporation rate is given by:
\f[
\hat{m_i} =
- C \rho_{g} D_{v,i}
\frac
{
\frac{dY_{v,i}}{dn}
}
{
1 - \; \sum_{1}^{Nv}Y_{g,j}
}
\f]
where:
\vartable
\hat{m_i} | mass flux rate [kg/s/m2]
\rho_{g} | gas phase density
D_{v,i} | diffusion coefficient
C | model coefficient
\frac{dY_{v,i}}{dn} | normal derivative of evaporated component
Y_{g,j} | mass fraction at the surface
\endvartable
Usage
Example usage:
\verbatim
massTransferModel
(
(liquid to gas)
{
// Mandatory entries
type diffusionGasEvaporation;
species vapour.gas;
C 1;
saturationPressure
{
type Antoine;
A 3.55;
B 643;
C -198;
}
// Optional entries
isoAlpha ;
Tactivate ;
// Inherited entries
...
}
);
\endverbatim
where:
\table
Property | Description | Type | Reqd | Deflt
type | Type name: diffusionGasEvaporation | word | yes | -
saturationPressure | Saturation model | dict | yes | -
isoAlpha | Iso-alpha for interface | scalar | no | 0.5
C | Model coefficient | scalar | yes | -
Tactivate | Saturation temperature | scalar | no | 0
\endtable
The inherited entries are elaborated in:
- \link InterfaceCompositionModel.H \endlink
- \link saturationModel.H \endlink
SourceFiles
diffusionGasEvaporation.C
\*---------------------------------------------------------------------------*/
#ifndef Foam_meltingEvaporationModels_diffusionGasEvaporation_H
#define Foam_meltingEvaporationModels_diffusionGasEvaporation_H
#include "InterfaceCompositionModel.H"
#include "saturationModel.H"
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * *//
namespace Foam
{
// Forward Declarations
class phasePair;
namespace meltingEvaporationModels
{
/*---------------------------------------------------------------------------*\
Class diffusionGasEvaporation Declaration
\*---------------------------------------------------------------------------*/
template
class diffusionGasEvaporation
:
public InterfaceCompositionModel
{
// Private Data
//- Saturation pressure model
autoPtr saturationModelPtr_;
//- Interface Iso-value
scalar isoAlpha_;
//- Evaporation coefficient
dimensionedScalar C_;
//- Activation temperature
const dimensionedScalar Tactivate_;
//- Interface area
volScalarField interfaceArea_;
//- Mass source
volScalarField mDotc_;
// Private Member Functions
//- Update interface
void updateInterface(const volScalarField& T);
public:
//- Runtime type information
TypeName("diffusionGasEvaporation");
// Constructors
//- Construct from components
diffusionGasEvaporation
(
const dictionary& dict,
const phasePair& pair
);
//- Destructor
virtual ~diffusionGasEvaporation() = default;
// Member Functions
//- Explicit total mass transfer coefficient
virtual tmp Kexp
(
const volScalarField& field
);
//- Implicit mass transfer coefficient
virtual tmp KSp
(
label modelVariable,
const volScalarField& field
);
//- Explicit mass transfer coefficient
virtual tmp KSu
(
label modelVariable,
const volScalarField& field
);
//- Return Tactivate
virtual const dimensionedScalar& Tactivate() const noexcept
{
return Tactivate_;
}
//- Add/subtract alpha*div(U) as a source term
//- for alpha, substituting div(U) = mDot(1/rho1 - 1/rho2)
virtual bool includeDivU() const noexcept
{
return true;
}
};
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
} // End namespace meltingEvaporationModels
} // End namespace Foam
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
#ifdef NoRepository
# include "diffusionGasEvaporation.C"
#endif
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
#endif
// ************************************************************************* //