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. 104, p. 42. 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. 104, p. 42.
Definition at line 52 of file Ergun.H.
Public Member Functions | |
TypeName ("Ergun") | |
Runtime type information.
| |
Ergun (const dictionary &interfaceDict, const volScalarField &alpha, const phaseModel &phasea, const phaseModel &phaseb) | |
Construct from components.
| |
virtual | ~Ergun () |
Destructor.
| |
tmp< volScalarField > | K (const volScalarField &Ur) const |
the dragfunction K used in the momentum eq.
|
Ergun | ( | const dictionary & | interfaceDict, |
const volScalarField & | alpha, | ||
const phaseModel & | phasea, | ||
const phaseModel & | phaseb | ||
) |
Construct from components.
virtual ~Ergun | ( | ) | [virtual]
|
Destructor.
TypeName | ( | "Ergun" | ) |
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.