Wall Porosity

The implementation of the VOF phase-specific wall porosity model is analogous to that of a porous baffle.

The velocity across the porous boundary is calculated from the known pressure drop across it.

This pressure drop is given as:

Figure 1. EQUATION_DISPLAY
Δp=-ρ(α|vn|+β)vn
(2641)

where ρ is the density of the phase, α and β are user supplied constants and vn is the normal velocity across the porous boundary. Simcenter STAR-CCM+ calculates the pressure drop from a specified external ambient pressure on the region. Eqn. (2641) is then applied to calculate the normal velocity. This normal velocity is used to predict the amount of mass leaving through the boundary face within a given time-step.

If a phase leaves the domain, the volume fraction is known. Under inflow conditions for multiple phases, the volume fraction is unknown as it is not solved for in the solid region. Therefore, the volume fraction must be assumed when fluid enters the domain through a porous wall boundary. It is assumed that phases are equally distributed: the volume fraction is equal to 1 for one phase, it is equal to 0.5 for two phases, it is equal to 0.333 for three phases, and so on.