|September 19, 2005, 14:45||
Dear all, I am using rhoTur
Join Date: Mar 2009
Posts: 101Rep Power: 8
I am using rhoTurbFoam for a pulsating channel application. The case consists of a heated pulsating air channel.
If I start my computations directly using rhoTurbFoam the solver needs a really small time step in order to reach a stable solution.
In order to obtain a faster solution I tought to initialize the field with a solution from turbFoam on the same cold pulsating channel.
After the turbFoam case reached the convergence, I added the temperature field and tried to run the case under rhoTurbFoam. The dimension for the pressure and phi were wrong and I simply changed them...
The calculation was anyway unstable and I got very soon nan values.
did I make a mistake?
Is that the right way to initialize the turbulent field from turbFoam to rhoTurbFoam?
The flow is incompressible ( very low mach number ) and the problem is of forced-convection type.. (not strong buoyance effects). Is rhoTurbFoam the right solver?
how can I improve its stability?
any advice will be apreciated,
|Thread||Thread Starter||Forum||Replies||Last Post|
|Turbulent compressible solver rhoTurbFoam with dynamic moving mesh||eno||OpenFOAM Running, Solving & CFD||4||December 12, 2011 04:38|
|RhoTurbFoam max number of iterations||jia_kok||OpenFOAM Running, Solving & CFD||6||July 3, 2009 05:03|
|RhoTurbFoam sonicFoam rhoSonicFoam||mwibmer||OpenFOAM Bugs||2||September 1, 2008 04:28|
|Problem: text commands to initialize flow field||Carolyn Jacobs||FLUENT||0||April 10, 2007 05:03|
|Putting submesh field values into field on parent mesh||helmut||OpenFOAM Running, Solving & CFD||2||June 20, 2006 07:31|