H, Enwald, E. Peirano, A-E Almstedt 'Eulerian Two-Phase Flow Theory Applied to Fluidization' Int. J. Multiphase Flow, Vol. 22, Suppl, pp. 21-66 (1996) Eq. 106, p. 43. More...
H, Enwald, E. Peirano, A-E Almstedt 'Eulerian Two-Phase Flow Theory Applied to Fluidization' Int. J. Multiphase Flow, Vol. 22, Suppl, pp. 21-66 (1996) Eq. 106, p. 43.
Definition at line 52 of file Gibilaro.H.
Public Member Functions | |
TypeName ("Gibilaro") | |
Runtime type information.
| |
Gibilaro (const dictionary &interfaceDict, const volScalarField &alpha, const phaseModel &phasea, const phaseModel &phaseb) | |
Construct from components.
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virtual | ~Gibilaro () |
Destructor.
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tmp< volScalarField > | K (const volScalarField &Ur) const |
the dragfunction K used in the momentum eq.
|
Gibilaro | ( | const dictionary & | interfaceDict, |
const volScalarField & | alpha, | ||
const phaseModel & | phasea, | ||
const phaseModel & | phaseb | ||
) |
Construct from components.
virtual ~Gibilaro | ( | ) | [virtual]
|
Destructor.
TypeName | ( | "Gibilaro" | ) |
Runtime type information.
tmp<volScalarField> K | ( | const volScalarField & | Ur ) | const [virtual]
|
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) NB ! ***************************** for numerical reasons alpha and beta has been extracted from the dragFunction K, so you MUST divide K by alpha*beta when implementing the drag function NB ! *****************************
Implements dragModel.