Public Member Functions | |
TypeName ("heatTransferModel") | |
Runtime type information. More... | |
declareRunTimeSelectionTable (autoPtr, heatTransferModel, dictionary,(const dictionary &interfaceDict, const volScalarField &alpha1, const phaseModel &phase1, const phaseModel &phase2),(interfaceDict, alpha1, phase1, phase2)) | |
heatTransferModel (const dictionary &interfaceDict, const volScalarField &alpha1, const phaseModel &phase1, const phaseModel &phase2) | |
virtual | ~heatTransferModel () |
Destructor. More... | |
virtual tmp< volScalarField > | K (const volScalarField &Ur) const =0 |
The heat-transfer function K used in the enthalpy eq. More... | |
TypeName ("heatTransferModel") | |
Runtime type information. More... | |
declareRunTimeSelectionTable (autoPtr, heatTransferModel, dictionary,(const dictionary &dict, const phasePair &pair),(dict, pair)) | |
heatTransferModel (const dictionary &dict, const phasePair &pair) | |
Construct froma dictionary and a phase pair. More... | |
virtual | ~heatTransferModel () |
Destructor. More... | |
tmp< volScalarField > | K () const |
The heat transfer function K used in the enthalpy equation. More... | |
virtual tmp< volScalarField > | K (const scalar residualAlpha) const =0 |
The heat transfer function K used in the enthalpy equation. More... | |
TypeName ("heatTransferModel") | |
Runtime type information. More... | |
declareRunTimeSelectionTable (autoPtr, heatTransferModel, dictionary,(const dictionary &dict, const phasePair &pair),(dict, pair)) | |
heatTransferModel (const dictionary &dict, const phasePair &pair) | |
Construct froma dictionary and a phase pair. More... | |
virtual | ~heatTransferModel () |
Destructor. More... | |
virtual tmp< volScalarField > | K () const =0 |
The heat transfer function K used in the enthalpy equation. More... | |
Static Public Member Functions | |
static autoPtr< heatTransferModel > | New (const dictionary &interfaceDict, const volScalarField &alpha1, const phaseModel &phase1, const phaseModel &phase2) |
static autoPtr< heatTransferModel > | New (const dictionary &dict, const phasePair &pair) |
static autoPtr< heatTransferModel > | New (const dictionary &dict, const phasePair &pair) |
Static Public Attributes | |
static const dimensionSet | dimK |
Coefficient dimensions. More... | |
Protected Attributes | |
const dictionary & | interfaceDict_ |
const volScalarField & | alpha1_ |
const phaseModel & | phase1_ |
const phaseModel & | phase2_ |
const phasePair & | pair_ |
Phase pair. More... | |
const dimensionedScalar | residualAlpha_ |
Residual phase fraction. More... | |
heatTransferModel | ( | const dictionary & | interfaceDict, |
const volScalarField & | alpha1, | ||
const phaseModel & | phase1, | ||
const phaseModel & | phase2 | ||
) |
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virtual |
Destructor.
heatTransferModel | ( | const dictionary & | dict, |
const phasePair & | pair | ||
) |
Construct froma dictionary and a phase pair.
|
virtual |
Destructor.
heatTransferModel | ( | const dictionary & | dict, |
const phasePair & | pair | ||
) |
Construct froma dictionary and a phase pair.
|
virtual |
Destructor.
TypeName | ( | "heatTransferModel" | ) |
Runtime type information.
declareRunTimeSelectionTable | ( | autoPtr | , |
heatTransferModel | , | ||
dictionary | , | ||
(const dictionary &interfaceDict, const volScalarField &alpha1, const phaseModel &phase1, const phaseModel &phase2) | , | ||
(interfaceDict, alpha1, phase1, phase2) | |||
) |
|
static |
|
pure virtual |
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! *****************************
Implemented in RanzMarshall.
TypeName | ( | "heatTransferModel" | ) |
Runtime type information.
declareRunTimeSelectionTable | ( | autoPtr | , |
heatTransferModel | , | ||
dictionary | , | ||
(const dictionary &dict, const phasePair &pair) | , | ||
(dict, pair) | |||
) |
|
static |
tmp<volScalarField> K | ( | ) | const |
The heat transfer function K used in the enthalpy equation.
ddt(alpha1*rho1*ha) + ... = ... K*(Ta - Tb) ddt(alpha2*rho2*hb) + ... = ... K*(Tb - Ta)
|
pure virtual |
The heat transfer function K used in the enthalpy equation.
ddt(alpha1*rho1*ha) + ... = ... K*(Ta - Tb) ddt(alpha2*rho2*hb) + ... = ... K*(Tb - Ta) with a specified residual volume fraction
Implemented in RanzMarshall, and sphericalHeatTransfer.
TypeName | ( | "heatTransferModel" | ) |
Runtime type information.
declareRunTimeSelectionTable | ( | autoPtr | , |
heatTransferModel | , | ||
dictionary | , | ||
(const dictionary &dict, const phasePair &pair) | , | ||
(dict, pair) | |||
) |
|
static |
|
pure virtual |
The heat transfer function K used in the enthalpy equation.
ddt(alpha1*rho1*ha) + ... = ... K*(Ta - Tb) ddt(alpha2*rho2*hb) + ... = ... K*(Tb - Ta)
Implemented in RanzMarshall, and sphericalHeatTransfer.
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protected |
Definition at line 56 of file heatTransferModel.H.
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protected |
Definition at line 57 of file heatTransferModel.H.
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protected |
Definition at line 58 of file heatTransferModel.H.
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protected |
Definition at line 59 of file heatTransferModel.H.
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protected |
Phase pair.
Definition at line 58 of file heatTransferModel.H.
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protected |
Residual phase fraction.
Definition at line 61 of file heatTransferModel.H.
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static |
Coefficient dimensions.
Definition at line 88 of file heatTransferModel.H.