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Remove non-ASCII characters

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Henry
2012-01-19 16:27:23 +00:00
parent fa9eb43280
commit 0b1bcbb753
11 changed files with 28 additions and 28 deletions
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4
applications/solvers/multiphase/compressibleTwoPhaseEulerFoam/interfacialModels/dragModels/dragModel/dragModel.H
View File

@ -114,11 +114,11 @@ public:
//- the dragfunction K used in the momentum eq.
// ddt(alpha*rhoa*Ua) + ... = ... alpha*beta*K*(Ua-Ub)
// ddt(beta*rhob*Ub) + ... = ... alpha*beta*K*(Ub-Ua)
// **********************************<EFBFBD>NB ! *****************************
// ********************************** NB! *****************************
// for numerical reasons alpha and beta has been
// extracted from the dragFunction K,
// so you MUST divide K by alpha*beta when implemnting the drag function
// **********************************<EFBFBD>NB ! *****************************
// ********************************** NB! *****************************
virtual tmp<volScalarField> K(const volScalarField& Ur) const = 0;
};

4
applications/solvers/multiphase/compressibleTwoPhaseEulerFoam/interfacialModels/heatTransferModels/heatTransferModel/heatTransferModel.H
View File

@ -114,12 +114,12 @@ public:
//- the heat-transfer function K used in the enthalpy eq.
// ddt(alpha*rhoa*ha) + ... = ... alpha*beta*K*(Ta - Tb)
// ddt(beta*rhob*hb) + ... = ... alpha*beta*K*(Tb - Ta)
// **********************************<EFBFBD>NB ! *****************************
// ********************************** NB!*****************************
// for numerical reasons alpha and beta has been
// extracted from the heat-transfer function K,
// so you MUST divide K by alpha*beta when implementing the
// heat-transfer function
// **********************************<EFBFBD>NB ! *****************************
// ********************************** NB!*****************************
virtual tmp<volScalarField> K(const volScalarField& Ur) const = 0;
};

4
applications/solvers/multiphase/interPhaseChangeFoam/phaseChangeTwoPhaseMixtures/Kunz/Kunz.H
View File

@ -35,8 +35,8 @@ Description
\verbatim
Kunz, R.F., Boger, D.A., Stinebring, D.R., Chyczewski, Lindau. J.W.,
Gibeling, H.J., Venkateswaran, S., Govindan, T.R.,
“A Preconditioned Implicit Method for Two-Phase Flows with Application
to Cavitation Prediction,”
"A Preconditioned Implicit Method for Two-Phase Flows with Application
to Cavitation Prediction,"
Computers and Fluids,
29(8):849-875, 2000.
\endverbatim

4
applications/solvers/multiphase/multiphaseEulerFoam/interfacialModels/dragModels/dragModel/dragModel.H
View File

@ -131,11 +131,11 @@ public:
//- the dragfunction K used in the momentum eq.
// ddt(alpha*rhoa*Ua) + ... = ... alpha*beta*K*(Ua-Ub)
// ddt(beta*rhob*Ub) + ... = ... alpha*beta*K*(Ub-Ua)
// **********************************<EFBFBD>NB ! *****************************
// ********************************** NB! *****************************
// for numerical reasons alpha and beta has been
// extracted from the dragFunction K,
// so you MUST divide K by alpha*beta when implemnting the drag function
// **********************************<EFBFBD>NB ! *****************************
// ********************************** NB! *****************************
virtual tmp<volScalarField> K(const volScalarField& Ur) const = 0;
};

4
applications/solvers/multiphase/multiphaseEulerFoam/interfacialModels/heatTransferModels/heatTransferModel/heatTransferModel.H
View File

@ -114,12 +114,12 @@ public:
//- the heat-transfer function K used in the enthalpy eq.
// ddt(alpha*rhoa*ha) + ... = ... alpha*beta*K*(Ta - Tb)
// ddt(beta*rhob*hb) + ... = ... alpha*beta*K*(Tb - Ta)
// **********************************<EFBFBD>NB ! *****************************
// ********************************** NB! *****************************
// for numerical reasons alpha and beta has been
// extracted from the heat-transfer function K,
// so you MUST divide K by alpha*beta when implementing the
// heat-transfer function
// **********************************<EFBFBD>NB ! *****************************
// ********************************** NB! *****************************
virtual tmp<volScalarField> K(const volScalarField& Ur) const = 0;
};

4
applications/solvers/multiphase/twoPhaseEulerFoam/interfacialModels/dragModels/dragModel/dragModel.H
View File

@ -114,11 +114,11 @@ public:
//- the dragfunction K used in the momentum eq.
// ddt(alpha*rhoa*Ua) + ... = ... alpha*beta*K*(Ua-Ub)
// ddt(beta*rhob*Ub) + ... = ... alpha*beta*K*(Ub-Ua)
// **********************************<EFBFBD>NB ! *****************************
// ********************************** NB ! *****************************
// for numerical reasons alpha and beta has been
// extracted from the dragFunction K,
// so you MUST divide K by alpha*beta when implemnting the drag function
// **********************************<EFBFBD>NB ! *****************************
// ********************************** NB ! *****************************
virtual tmp<volScalarField> K(const volScalarField& Ur) const = 0;
};