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

Species Transport Model

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   July 30, 2013, 02:20
Default Species Transport Model
  #1
New Member
 
Join Date: Jul 2013
Posts: 1
Rep Power: 0
srinag is on a distinguished road
Hi, I've been trying to simulate reacting flow in a model combustor. Realizable k-e model is used for turbulence modeling and Finite rate eddy dissipation model is used for combustion. The constants such as the Prandtl & Schmid numbers are retained as default values. The temperature predicted is about 400K higher than the experimental results. Can anyone pl suggest me the modifications that could be done to obtain a lower temperature.

Thanks in advance.
srinag is offline   Reply With Quote

Old   August 1, 2013, 16:41
Default
  #2
Senior Member
 
A CFD free user's Avatar
 
A-A Azarafza
Join Date: Jan 2013
Posts: 226
Rep Power: 14
A CFD free user is on a distinguished road
Quote:
Originally Posted by srinag View Post
Hi, I've been trying to simulate reacting flow in a model combustor. Realizable k-e model is used for turbulence modeling and Finite rate eddy dissipation model is used for combustion. The constants such as the Prandtl & Schmid numbers are retained as default values. The temperature predicted is about 400K higher than the experimental results. Can anyone pl suggest me the modifications that could be done to obtain a lower temperature.

Thanks in advance.
Hello
Why do you use finite rate model? In this case, turbulent flow is ignored, because finite rate model is used when the kinetic is reaction controlling. If the flow is turbulent, you should use finite rate/eddy dissipation rate model. In this case, if the kinetic is controlling, then, finite rate model is applied and on the other hand, when the turbulency is controlling, then eddy dissipation model is used. So I suppose that you should change the reaction model.
__________________
Regard yours
A CFD free user is offline   Reply With Quote

Old   October 6, 2013, 13:30
Default
  #3
New Member
 
sofiane ouali
Join Date: Oct 2013
Posts: 3
Rep Power: 13
potion is on a distinguished road
hi!
see material panel in first and change default value
in second time, you can change cte A and B of Ahrenius law in reaction panel
potion 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
Please help!! Patch and Species transport Julie FLUENT 5 August 3, 2016 04:10
Divergence problem for species transport model MY FLUENT 3 January 11, 2014 05:46
chemical reaction and species transport mohamad3564 FLUENT 0 June 11, 2012 04:58
Implement species transport equation Tobi OpenFOAM Programming & Development 0 June 2, 2012 14:26
species transport model or mixture model? achaokaoyan Main CFD Forum 0 July 10, 2010 11:52


All times are GMT -4. The time now is 03:53.