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STYLE: twoPhaseEulerFoam: updated interfacial model headers to reflect changes in the definition of K

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This commit is contained in:
william
2014-03-18 09:07:35 +00:00
committed by Andrew Heather
parent cfdd46ef15
commit e71b49311c
8 changed files with 14 additions and 28 deletions
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9
applications/solvers/multiphase/twoPhaseEulerFoam/interfacialModels/dragModels/dragModel/dragModel.H
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@ -134,13 +134,8 @@ public:
virtual tmp<volScalarField> CdRe() const = 0;
//- The drag function K used in the momentum equation
// ddt(alpha1*rho1*U1) + ... = ... alpha1*alpha2*K*(U1-U2)
// ddt(alpha2*rho2*U2) + ... = ... alpha1*alpha2*K*(U2-U1)
// ********************************** NB! *****************************
// for numerical reasons alpha1 and alpha2 has been extracted from the
// drag function K, so you MUST divide K by alpha1*alpha2 when
// implemnting the drag function
// ********************************** NB! *****************************
// ddt(alpha1*rho1*U1) + ... = ... K*(U1-U2)
// ddt(alpha2*rho2*U2) + ... = ... K*(U2-U1)
virtual tmp<volScalarField> K() const;
//- Dummy write for regIOobject

2
applications/solvers/multiphase/twoPhaseEulerFoam/interfacialModels/heatTransferModels/RanzMarshall/RanzMarshall.H
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@ -47,7 +47,7 @@ namespace heatTransferModels
{
/*---------------------------------------------------------------------------*\
Class RanzMarshall Declaration
Class RanzMarshall Declaration
\*---------------------------------------------------------------------------*/
class RanzMarshall

11
applications/solvers/multiphase/twoPhaseEulerFoam/interfacialModels/heatTransferModels/heatTransferModel/heatTransferModel.H
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@ -46,7 +46,7 @@ namespace Foam
class phasePair;
/*---------------------------------------------------------------------------*\
Class heatTransferModel Declaration
Class heatTransferModel Declaration
\*---------------------------------------------------------------------------*/
class heatTransferModel
@ -115,13 +115,8 @@ public:
// Member Functions
//- The heat transfer function K used in the enthalpy equation
// 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!*****************************
// ddt(alpha1*rho1*ha) + ... = ... K*(Ta - Tb)
// ddt(alpha2*rho2*hb) + ... = ... K*(Tb - Ta)
virtual tmp<volScalarField> K() const = 0;
};

2
applications/solvers/multiphase/twoPhaseEulerFoam/interfacialModels/turbulentDispersionModels/noTurbulentDispersion/noTurbulentDispersion.H
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@ -47,7 +47,7 @@ namespace turbulentDispersionModels
{
/*---------------------------------------------------------------------------*\
Class noTurbulentDispersion Declaration
Class noTurbulentDispersion Declaration
\*---------------------------------------------------------------------------*/
class noTurbulentDispersion

2
applications/solvers/multiphase/twoPhaseEulerFoam/interfacialModels/virtualMassModels/constantVirtualMassCoefficient/constantVirtualMassCoefficient.H
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@ -48,7 +48,7 @@ namespace virtualMassModels
{
/*---------------------------------------------------------------------------*\
Class constantVirtualMassCoefficient Declaration
Class constantVirtualMassCoefficient Declaration
\*---------------------------------------------------------------------------*/
class constantVirtualMassCoefficient

3
applications/solvers/multiphase/twoPhaseEulerFoam/interfacialModels/virtualMassModels/noVirtualMass/noVirtualMass.H
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@ -47,7 +47,7 @@ namespace virtualMassModels
{
/*---------------------------------------------------------------------------*\
Class noVirtualMass Declaration
Class noVirtualMass Declaration
\*---------------------------------------------------------------------------*/
class noVirtualMass
@ -80,6 +80,7 @@ public:
//- Virtual mass coefficient
virtual tmp<volScalarField> Cvm() const;
//- The virtual mass function K used in the momentum equation
virtual tmp<volScalarField> K() const;
};

11
applications/solvers/multiphase/twoPhaseEulerFoam/interfacialModels/virtualMassModels/virtualMassModel/virtualMassModel.H
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@ -47,7 +47,7 @@ namespace Foam
class phasePair;
/*---------------------------------------------------------------------------*\
Class virtualMassModel Declaration
Class virtualMassModel Declaration
\*---------------------------------------------------------------------------*/
class virtualMassModel
@ -120,13 +120,8 @@ public:
virtual tmp<volScalarField> Cvm() const = 0;
//- The virtual mass function K used in the momentum equation
// ddt(alpha1*rho1*U1) + ... = ... alpha1*alpha2*K*(DU1_Dt - DU2_Dt)
// ddt(alpha2*rho2*U2) + ... = ... alpha1*alpha2*K*(DU1_Dt - DU2_Dt)
// ********************************** NB! *****************************
// for numerical reasons alpha1 and alpha2 has been extracted from the
// virtual mass function K, so you MUST divide K by alpha1*alpha2 when
// implemnting the virtual mass function
// ********************************** NB! *****************************
// ddt(alpha1*rho1*U1) + ... = ... K*(DU1_Dt - DU2_Dt)
// ddt(alpha2*rho2*U2) + ... = ... K*(DU1_Dt - DU2_Dt)
virtual tmp<volScalarField> K() const;
// Dummy write for regIOobject

2
applications/solvers/multiphase/twoPhaseEulerFoam/interfacialModels/wallLubricationModels/wallLubricationModel/wallLubricationModel.H
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@ -47,7 +47,7 @@ namespace Foam
class phasePair;
/*---------------------------------------------------------------------------*\
Class wallLubricationModel Declaration
Class wallLubricationModel Declaration
\*---------------------------------------------------------------------------*/
class wallLubricationModel