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

DPM Diameter querry

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   August 16, 2010, 22:00
Default DPM Diameter querry
  #1
Senior Member
 
Mohsin Mukhtar
Join Date: Mar 2010
Location: South Korea
Posts: 249
Rep Power: 17
Mohsin is on a distinguished road
I am using DPM surface injection from inlet whose sides are 0.82*0.89 m. But when i inject particles of 10 m diameter still i get the resullt at the outlet. why is it so??? How can a particle enter into a duct having bigger dimensions than the duct? Aren't I supposed to get an error??

Your urgent response will be highly appreciated.

Mohsin
Mohsin is offline   Reply With Quote

Old   August 16, 2010, 22:37
Default
  #2
Senior Member
 
xrs333
Join Date: Aug 2010
Posts: 125
Rep Power: 16
xrs333 is on a distinguished road
DPM model is a Euler-Lagrangian multiphase flow model, that is, the discrete phase is considered as particles no matter how big it is, only the trajectory of the centroid is cumputed.
xrs333 is offline   Reply With Quote

Old   August 16, 2010, 22:43
Default
  #3
Senior Member
 
Mohsin Mukhtar
Join Date: Mar 2010
Location: South Korea
Posts: 249
Rep Power: 17
Mohsin is on a distinguished road
Thanks for your reply

As far as i know in the langrangian method the particles are tracked while in Eulerian method fixed point is taken and particles are not followed.

Dpm uses Langrangian formulation but How can a trajectory be calculated if the diameter of the particle is larger than the duct in which it is moving? could u please elaborate.
Mohsin is offline   Reply With Quote

Old   August 16, 2010, 23:00
Default
  #4
Senior Member
 
xrs333
Join Date: Aug 2010
Posts: 125
Rep Power: 16
xrs333 is on a distinguished road
In real world it is impossible for the diameter of a particle larger than the duct. So, in the computer, if you build a computation model like that, the mistake is brought about by you, not by the computer or the DPM model. You built a wrong model with a improper method.
xrs333 is offline   Reply With Quote

Old   August 16, 2010, 23:04
Default
  #5
Senior Member
 
Mohsin Mukhtar
Join Date: Mar 2010
Location: South Korea
Posts: 249
Rep Power: 17
Mohsin is on a distinguished road
ok so i will assign the diameters according to the streams I m sending in. for exapmple for group injection of 5 streams in a duct of 5m, I will assign a diameter starting to end point as 0.1 so that each particle stream has 0.1 diameter and it should remian in the domain. otherwise if i assign a diameter of 0.2 fluent will still calualte it but as u mentioned it would contradict with the real world problem and would have errors.

If i m wrong please let me know. Thanks for your time.
Mohsin 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
DPM diameter mass distribution Wouter FLUENT 5 May 23, 2019 02:18
Importance of Hydraulic Diameter Value for Compressible Flow RyGuy FLUENT 0 August 6, 2009 10:58
DPM - do the particles affect the liquid? Nikhil Dani FLUENT 0 January 1, 2009 11:58
The minimum diameter of second phase in the DPM Fluenter FLUENT 2 August 15, 2004 06:46
DPM - setting the density and diameter Christian Svensson FLUENT 0 February 14, 2003 13:44


All times are GMT -4. The time now is 01:52.