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

Should I be using True or Superficial Velocity for Porous Domain?

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   November 16, 2010, 07:29
Default Should I be using True or Superficial Velocity for Porous Domain?
  #1
siw
Senior Member
 
Stuart
Join Date: Jul 2009
Location: Portsmouth, England
Posts: 742
Rep Power: 26
siw will become famous soon enough
Hi,

I've measured the pressure loss (del_p) across an air filter as a function of volumetric flow flow (Q) in the laboratory using a real air filter. I've plotted the data and got a 2nd-order polynimal equation, with coefficients A and B:

del_p = (A * Q) + (B * Q^2)

I've then calculated an average velocity (V_ave) across the air filter as a function of the volumetric flow rate. So now I have an equation:

del_p = (C * V_ave) + (D * V_ave^2)

where the coefficients C and D have different values to A and B.

So what I'd like to know is if I should be using the True or Superficial velocity model? I think true velocity because I started with experiemental data from a real air filter but I'm also thinking Superficial velocity because my final coefficients have used an averaged velocity. No doubt I'll try both, but I'd like some understanding from the CFX community.

Thanks.

Last edited by siw; November 16, 2010 at 07:31. Reason: Typo
siw is offline   Reply With Quote

Old   November 17, 2010, 06:36
Default
  #2
Senior Member
 
Matthias Voß
Join Date: Mar 2009
Location: Berlin, Germany
Posts: 449
Rep Power: 20
mvoss is on a distinguished road
hi

superficial velocities are derived from the velocities and the volume fractions. Do you follow a multiphase approach?

neewbie
mvoss is offline   Reply With Quote

Old   November 17, 2010, 08:52
Default
  #3
siw
Senior Member
 
Stuart
Join Date: Jul 2009
Location: Portsmouth, England
Posts: 742
Rep Power: 26
siw will become famous soon enough
Hi,

This is for single phase (air) only. I'm going to neglect the particles that the air filter removes for this particular simulation.
siw is offline   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
porous rotating solid domain kiran choudar FLUENT 1 March 1, 2021 09:55
Radiation at interface between fluid and porous domain Hitch8 CFX 19 April 20, 2015 07:24
Heat transfer in porous domain CFX V12 Hashmi CFX 0 August 15, 2009 13:05
physical velocity formulation and porous media KLG FLUENT 2 June 10, 2003 11:14
Terrible Mistake In Fluid Dynamics History Abhi Main CFD Forum 12 July 8, 2002 10:11


All times are GMT -4. The time now is 18:17.