Rather than forcing the dispersed-phase velocity -> the continuous-phase velocity as the phase-fraction -> 0 the velocity is now calculated from a balance of pressure, buoyancy and drag forces. The advantage is now liquid or particles are not carried out of bubble-column of fluidised-beds by the fictitious drag caused by forcing the phase-velocities becoming equal in the limit. |
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|---|---|---|
| .. | ||
| cavitatingFoam | ||
| compressibleInterFoam | ||
| compressibleMultiphaseInterFoam | ||
| driftFluxFoam | ||
| interFoam | ||
| interPhaseChangeFoam | ||
| multiphaseEulerFoam | ||
| multiphaseInterFoam | ||
| potentialFreeSurfaceFoam | ||
| twoLiquidMixingFoam | ||
| twoPhaseEulerFoam | ||