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| TypeName ("heatTransferModel") |
| Runtime type information. More...
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| declareRunTimeSelectionTable (autoPtr, heatTransferModel, dictionary,(const dictionary &dict, const volScalarField &alpha1, const phaseModel &phase1, const phaseModel &phase2),(dict, alpha1, phase1, phase2)) |
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| heatTransferModel (const dictionary &dict, const volScalarField &alpha1, const phaseModel &phase1, const phaseModel &phase2) |
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virtual | ~heatTransferModel ()=default |
| Destructor. More...
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virtual tmp< volScalarField > | K (const volScalarField &Ur) const =0 |
| The heat-transfer function K used in the enthalpy eq. More...
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- Source files
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Definition at line 51 of file heatTransferModel.H.
◆ heatTransferModel()
◆ ~heatTransferModel()
◆ TypeName()
TypeName |
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"heatTransferModel" |
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Runtime type information.
◆ declareRunTimeSelectionTable()
declareRunTimeSelectionTable |
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autoPtr |
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heatTransferModel |
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dictionary |
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(const dictionary &dict, const volScalarField &alpha1, const phaseModel &phase1, const phaseModel &phase2) |
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(dict, alpha1, phase1, phase2) |
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◆ New()
◆ K()
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.
◆ interfaceDict_
◆ alpha1_
◆ phase1_
◆ phase2_
The documentation for this class was generated from the following files:
- src/phaseSystemModels/multiphaseEuler/multiphaseSystem/interfacialModels/heatTransferModels/heatTransferModel/heatTransferModel.H
- src/phaseSystemModels/multiphaseEuler/multiphaseSystem/interfacialModels/heatTransferModels/heatTransferModel/heatTransferModel.C