 |
 |
 |
|
|
|
[Sponsors] | ||||
September 17, 2002, 06:44
|
About gas-liquid flow and turbulence
|
#1 |
|
Guest
Posts: n/a
|
Hi everybody, I'm studying airlift loop reactor and I've noticed that it was important to consider multiphase-turbulence-model by abling interphase momentum source. So I wanted to know when can I able this stuff ? I mean , must I wait that the 1st order with loose mesh is converged (before refining) ? Or do I have to able it at the beginning, knowing convergence will be difficult to reach ??
Thanx for answering |
|
|
||
 |
| Thread Tools | Search this Thread |
| Display Modes | |
|
|
Similar Threads
|
||||
| Thread | Thread Starter | Forum | Replies | Last Post |
| mass flow in is not equal to mass flow out | saii | CFX | 12 | March 19, 2018 06:21 |
| Constant velocity of the material | Sas | CFX | 15 | July 13, 2010 09:56 |
| Discussion: Reason of Turbulence!! | Wen Long | Main CFD Forum | 3 | May 15, 2009 10:52 |
| Code release: Flow Transition and Turbulence | Chaoqun Liu | Main CFD Forum | 0 | September 26, 2008 18:15 |
Linear Mode
