CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > ANSYS > FLUENT

pressure drop in porous media

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   December 15, 2003, 15:42
Default pressure drop in porous media
  #1
Dongying Qian
Guest
 
Posts: n/a
Hi,guys:

I am modelling single phase flow in porous media region and want to get the pressure drop. The case is 2d, 0.5x60 mm dimension with water liquid as the fluid media. The inlet is uniform velocity 0.0667 m/s and outlet is zero pressure. Since it is laminar, i only set the viscous resistance 1.5e11 for each direction. I found an interesting phenomenon: the pressure drop depends on the mesh fineness dramatically (several order of the magnitude)! For example, i have used uniform mesh with size 50, and got 6.0e5 Pa pressure drop. However, if i set the boundary layer with starting size 10 or 20, and 4 ~ 5 grouth layers, the pressure drop is 2 or 3 order of magnitude bigger. Beside, the velocity field is flat, same almost everywhere except the boundary point. Anybody have an idea? If somebody has interest, you can test it very quickly. Please help me out. Thanks.

Janice
  Reply With Quote

Old   December 16, 2003, 05:14
Default Re: pressure drop in porous media
  #2
Erwin
Guest
 
Posts: n/a
Do you think a pressure loss of 6 bar over a length of just 6 cm with laminar flow is realistic? What kind of porous media is this supposed to be?

At least it explains why the velocity field is completely flat, don't you think?
  Reply With Quote

Old   December 16, 2003, 10:45
Default Re: pressure drop in porous media
  #3
Dongying Qian
Guest
 
Posts: n/a
The unit is Pa, not bar.
  Reply With Quote

Old   December 17, 2003, 06:06
Default Re: pressure drop in porous media
  #4
Erwin
Guest
 
Posts: n/a
6.0e5 Pa = 6 bar
  Reply With Quote

Old   January 2, 2004, 15:38
Default Re: pressure drop in porous media
  #5
mystic_cfd
Guest
 
Posts: n/a
Hi Janice

i have 2 suggestions:

1) Could you check your grid when you use a different BL resolution - make sure that you do not accidentally change the length of the porous region (change the physical length of the porous zone).

2) What are your convergence criteria - do you run the solution to machine accuracy, or do you use the standard 1e-3 convergence limit. For such small geometry you should check the influence of the convergence criteria on the pressure drop. and use 2nd order discretization.

cheers
  Reply With Quote

Reply


Posting Rules
You may not post new threads
You may not post replies
You may not post attachments
You may not edit your posts

BB code is On
Smilies are On
[IMG] code is On
HTML code is Off
Trackbacks are Off
Pingbacks are On
Refbacks are On


Similar Threads
Thread Thread Starter Forum Replies Last Post
Pressure drag problem in porous media with interFoam skp OpenFOAM Running, Solving & CFD 8 May 27, 2015 09:10
porous pressure drop. Bugs? whiz FLUENT 5 March 16, 2010 20:18
Pressure drop of valve with valve opening of 30% elogesh Main CFD Forum 2 January 5, 2007 13:30
BIG TROUBLE with heat exchanger and porous media!! Andrea FLUENT 0 February 20, 2005 08:49
Hydrostatic pressure in 2-phase flow modeling (CFX4.2) HB &DS CFX 0 January 9, 2000 14:19


All times are GMT -4. The time now is 11:40.