CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > OpenFOAM > OpenFOAM Running, Solving & CFD

LES: Turbulent Channel Flow without initial solution (BC)

Register Blogs Community New Posts Updated Threads Search

Like Tree18Likes

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   September 6, 2013, 05:10
Default
  #21
New Member
 
Danesh S
Join Date: Jul 2013
Location: Bochum, Germany
Posts: 27
Rep Power: 12
DaSh is on a distinguished road
To be closed. Thanks.

Last edited by DaSh; September 13, 2013 at 04:32.
DaSh is offline   Reply With Quote

Old   February 8, 2015, 16:09
Default
  #22
Member
 
Ali Shamooni
Join Date: Oct 2010
Posts: 44
Rep Power: 15
Alish1984 is on a distinguished road
Quote:
Originally Posted by Lieven View Post
Hi Danesh,


Were you already using the channelFoam solver? Cause based on the fact that you mentioned you were using RAS profiles I assumed you were not (channelFoam accepts only LES turbulence models). If you are, you are correct the pressure gradient should be imposed already based on comparing the actual mean flow rate with the requested mean flow rate (from the transportProperties).

But if you are using pisoFoam, you need to include tis pressure gradient yourself in the equation. You can follow either this approach, so imposing a flow rate, or you can directly set 'gradP' as a fixed value.

Cheers,

Lieven

Dear Lieven

Is it possible to solve a nozzle with the concept used in the channelFoam?
I mean I guess cyclicBC & gradpPlus used in the solver is the combination that generates turbulence in your field when using LES. If I am wrong tell me.
When the area in the inlent and outlet are not the same, then u cant use cyclic. without cyclicBC and using channelFoam it is likely to end up in a Poiseuille flow result (by using pisoFoam),
Then how can u solve this problem. I mean simulation of flow in a nozzle using LES.

Regards

Ali
Alish1984 is offline   Reply With Quote

Reply

Tags
channel flow, convergence, initial condition, les


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
Floating point exception error Alan OpenFOAM Running, Solving & CFD 11 July 1, 2021 21:51
pimpleFoam: turbulence->correct(); is not executed when using residualControl hfs OpenFOAM Running, Solving & CFD 3 October 29, 2013 08:35
How to write k and epsilon before the abnormal end xiuying OpenFOAM Running, Solving & CFD 8 August 27, 2013 15:33
pisoFoam - unstable pressure residual Industrial_CFD OpenFOAM Running, Solving & CFD 21 February 24, 2013 15:39
Orifice Plate with a fully developed flow - Problems with convergence jonmec OpenFOAM Running, Solving & CFD 3 July 28, 2011 05:24


All times are GMT -4. The time now is 19:50.