|
[Sponsors] |
May 14, 2024, 16:16 |
porous media
|
#1 |
New Member
Daniel
Join Date: Oct 2023
Posts: 4
Rep Power: 2 |
Good day. I'm having a problem that I didn't use to have. When configuring a volume as a porous medium, I use the term linear and quadratic to simulate the resistance to flow. This causes a pressure drop and should cause a deceleration of the fluid as it passes through the pore volume.
It turns out that the simulation is giving me the opposite: the fluid is accelerating as it passes the porous medium. The pressure drops as expected. But the velocity of the fluid is increasing. I tried changing the streamwise direction vector to (-1) but nothing works. The fluid does not slow down. I appreciate any help. |
|
May 14, 2024, 17:37 |
|
#2 | |
Senior Member
Join Date: Jun 2009
Posts: 1,816
Rep Power: 32 |
Quote:
If you have an open medium, say fluid domain, and it enters a porous media and you use local/true velocity formulation the velocity will INCREASE regardless of the pressure drop. True/Local Velocity = Superficial Velocity / Volume Porosity
__________________
Note: I do not answer CFD questions by PM. CFD questions should be posted on the forum. |
||
May 14, 2024, 18:22 |
|
#3 |
New Member
Daniel
Join Date: Oct 2023
Posts: 4
Rep Power: 2 |
Thanks for your answer. Using any formulation (true or superficial) in the porous medium setup, I get the same response. It accelerates.
|
|
May 15, 2024, 12:06 |
|
#4 |
Senior Member
Erik
Join Date: Feb 2011
Location: Earth (Land portion)
Posts: 1,171
Rep Power: 23 |
Why would it decelerate? That should not ever happen depending on geometry.
Even Superficial velocity would remain constant in a continuum of incompressible flow. Are you using a compressible fluid? If so, pressure drop causes reduced density and therefore acceleration of the fluid. If this isn't it, then we need more info regarding your geometry and setup: Are you using a general loss subdomain in your fluid domain, or a Separate Porous Domain? If the latter what are you using for Volume Porosity, superficial/true velocity specification, and values. |
|
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
Thermal non-equilibrium porous media model with conjugate heat transfer | Hexahedron | FLUENT | 9 | February 22, 2023 02:55 |
Porous Media Zone Thickness | TheKitchenCleaner | FLUENT | 0 | October 5, 2020 00:42 |
Porous media setup issues in Fluent | Bernard Van | FLUENT | 29 | January 26, 2017 04:09 |
How to model granular flow through porous media | Axius | FLUENT | 2 | August 7, 2014 10:34 |
porous media: Fluent or Star-CD? | Igor | Main CFD Forum | 0 | December 5, 2002 15:16 |