Base class for film heat transfer models. More...


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... | |
Base class for film heat transfer models.
Definition at line 50 of file heatTransferModel.H.
| heatTransferModel | ( | const dictionary & | interfaceDict, |
| const volScalarField & | alpha1, | ||
| const phaseModel & | phase1, | ||
| const phaseModel & | phase2 | ||
| ) |
|
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.
|
protected |
Definition at line 56 of file heatTransferModel.H.
|
protected |
Definition at line 57 of file heatTransferModel.H.
|
protected |
Definition at line 58 of file heatTransferModel.H.
|
protected |
Definition at line 59 of file heatTransferModel.H.
|
protected |
Phase pair.
Definition at line 58 of file heatTransferModel.H.
|
protected |
Residual phase fraction.
Definition at line 61 of file heatTransferModel.H.
|
static |
Coefficient dimensions.
Definition at line 88 of file heatTransferModel.H.
1.8.11