$FOAM_TUTORIALS/incompressible/porousSimpleFoam/straightDuctImplicit
We calculate a flow with a porous media that models a filter in the middle of the flow path. The fluid flows in from the region "inlet" (X minimum plane) at a volumetric flow rate of 0.1 m3/s, passes through the filter (red part), and flows out from the region "outlet" (X maximum plane).
Porous media depends on the Darcy-Forchheimer law , and for a flow velocity ui (i=x, y, z) in direction i, a generation term Si (pressure drop) in the opposite direction of flow is added to the Navier-Stokes equations. Here, μ is the viscosity coefficient and ρ is the density.
The parameters that determine the properties of the porous media, Dij, F, the direction of the properties, and the region in which the porous media, are specified in the file constant/porosityProperties as follows.
porosity1 { type DarcyForchheimer; active yes; cellZone porosity; DarcyForchheimerCoeffs { d (5e7 -1000 -1000); f (0 0 0); coordinateSystem { type cartesian; origin (0 0 0); coordinateRotation { type axesRotation; e1 (1 0 0); e2 (0 0 1); } } } }
The standard k-ε model is used for the turbulence model.
The meshes are as follows, and the number of mesh is 16016. We use foamyHexMesh to create the mesh.
If you want to visualize turbulent energy and turbulent dissipation rate, check "k" and "epsilon" in the "Properties" tab in ParaView.
The calculation result is as follows.
We can see that the flow velocity and pressure are greatly reduced in the porous media part.
*Single, Core(TM) i7-2600 CPU @ 3.40GHz 3.40GHz