Please inclu Hello everyone,
d4.mfx (10.5 KB)
I am working on a cold-flow bubbling fluidized bed simulation using MFiX-TFM with Cartesian cut-cell geometry. The experimental bed is a narrow vertical cylinder with an inner diameter of 0.06 m and a height of 1.4 m. The initial packed bed height is about 0.16 m. The particle diameter range is approximately 0.35–1.0 mm.
I have several questions about the computational domain, geometry setup, mesh resolution, cut-cell tolerances, and wall boundary conditions.
1. Computational domain size in X and Z directions
For a cylindrical bed with radius 0.03 m, should the computational domain in the X and Z directions be exactly:
X: -0.03 to 0.03 mZ: -0.03 to 0.03 m
or should it be slightly larger than the cylinder radius, for example:
X: -0.033 to 0.033 mZ: -0.033 to 0.033 m
I am not sure whether the domain boundary should coincide with the cylinder surface or whether a small clearance is recommended for Cartesian cut-cell meshing.
2. Which geometry setup is recommended?
I am considering two possible ways to define the cylindrical wall:
Option A: Use an STL cylinder and define the wall as a Cartesian grid boundary condition using the imported STL surface.
Option B: Use a built-in procedural or primitive cylinder directly inside MFiX.
For a simple cylindrical fluidized bed, which approach is generally more robust for Cartesian cut-cell meshing?
Also, when using the STL geometry, I saw the “Select facets (STL)” option in the boundary condition panel. Should I check inside?
3. Mesh resolution for particles of 0.35–1.0 mm
The particle diameter range is 0.35–1.0 mm. For a bed diameter of 0.06 m, I have tried different background mesh resolutions in X and Z. For example:
20 × 400 × 2016 × 328 × 1630 × 328 × 30
However, the cut-cell mesh sometimes produces small cells or high-aspect-ratio cells near the cylindrical wall, and this can lead to local high velocities or convergence issues.
For this type of narrow cylindrical bubbling bed, what mesh resolution would you recommend in the radial directions and height direction?
Should I aim for a mesh size close to several particle diameters, or should I mainly avoid very small cut cells near the wall?
4. Cut-cell tolerance settings
I have tested different values for the cut-cell mesher tolerances, such as:
Small cell toleranceSmall area toleranceSnap tolerance in X/Y/ZNormal distance tolerance
Sometimes increasing the small cell tolerance and snap tolerance removes bad small cells and improves the mesh. However, in some cases the cylinder shape appears slightly distorted, for example the top or bottom circular edge looks truncated or flattened.
Could you please explain why changing these tolerance values sometimes changes the apparent geometry shape, while in other cases it does not?
Could you suggest a reasonable high-quality starting set of cut-cell tolerance parameters for this geometry?
For example, would the following be reasonable, or too aggressive?
Small cell tolerance: 0.05Small area tolerance: 0.05Snap tolerance X/Y/Z: 0.05–0.10Normal distance tolerance: 0.0
I would like to remove problematic tiny cut cells without significantly distorting the cylindrical wall.
5. Wall boundary condition for a smooth and narrow experimental bed
My experimental cylindrical pipe wall is relatively smooth, and the bed is narrow. I am concerned that a no-slip wall condition may strongly affect bed expansion and bubble behavior.
In the Cartesian-grid STL wall boundary condition, I can define the wall as CG_PSW, but I am not sure whether partial-slip or free-slip settings are available in this case.
Can a Cartesian-grid STL wall be set as partial-slip or free-slip for the solids phase? If not, what is the recommended wall boundary condition for a smooth acrylic or glass narrow fluidized bed?
Would using a no-slip wall condition likely suppress particle motion near the wall and affect the predicted bed expansion height?
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Thank you very much for your help and suggestions.de project files - Main menu/Submit bug report - attach zip file here.




