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

Under relaxation factors

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   January 28, 2005, 17:37
Default Under relaxation factors
  #1
MP
Guest
 
Posts: n/a
Hi,

I am solving a non-linear system of temperature and species equations (arrehinous terms for chemical reactions included as udfs). The system involves high temperature calculations. The soultion diverges even at under relaxation settings of 0.05 for temperature and species. Is it ok to use such low or even lower values of URs? Are there other ways of ensuring a converged soluton (I have checked denser grids as well).

Manan
  Reply With Quote

Old   January 30, 2005, 09:54
Default Re: Under relaxation factors
  #2
Swarup
Guest
 
Posts: n/a
Hi,

for species transport due to convection, URF should be 0.05. for heat transfer, it is advisable to use as small URF as possible for enthalpy. you can try even lower URF for enthalpy.

Swarup.
  Reply With Quote

Old   January 30, 2005, 10:46
Default Re: Under relaxation factors
  #3
MP
Guest
 
Posts: n/a
Hi Swarup,

Thanks for the advice. I have tried even lower URFs (0.005) but I still get divergence on reducing thermal conductivity values. Actually I am presently using higher than reality values of thermal conductivity to ensure convergence. But, on reducing K values, I get divergence which I think is due to high level of nonlinearity(exponential rate terms) in the my equations.

Can you or anyone else advice me on how to ensure further convergence.

Manan
  Reply With Quote

Old   January 30, 2005, 11:11
Default Re: Under relaxation factors
  #4
Swarup
Guest
 
Posts: n/a
Hi Manan,

the only way i can think as of now is that you should linearize your source term. it is likely that this has already been done for you in the FLUENT code. this will be an approximation for actual situation but may work.

How to do it i have little idea as of now and will be able to tell you later.

you may be knowing that a source term can be linearized using the approximation S=Sc+(phi)Sp where Sp should be -ve for stability purposes.

in my opinion, you should consult manual for reaction modeling or relaxation factors for discussion on coupling of enthalpy equation and species transport equation or even better can ask FLUENT support team itself.

Best of luck and regards, Swarup.
  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
Relaxation Factors for Transient solvers philippose OpenFOAM Running, Solving & CFD 19 March 20, 2014 04:39
Purpose of relaxation factors Mohsin FLUENT 5 April 30, 2010 11:57
relaxation factors and time accuracy Mike Main CFD Forum 7 May 21, 2005 12:41
Relaxation Factors Tim Phoenics 3 June 30, 2004 02:03
relaxation factors adjust zhujianguo Phoenics 1 July 15, 2003 11:11


All times are GMT -4. The time now is 21:34.