|May 19, 2010, 06:27||
Flow at different temperatures
Join Date: Oct 2009
Posts: 18Rep Power: 7
i'm dealing with a multiphase transient model which contains two gas and a solid divided in tiny particles. The two gas are injected against the solid, which is contained in a kind of vessel, so the solid particles are drag with the flow.
I've ran the simulation at enviromental conditions as an isotermal process at 25 C and it works. The problem comes when the temperature of my isothermal problem is changed to 700 C instead of 25. The solver gets the solution but now it seems the solid particles are thrown out of the reactor and i don't understand it, because if the temperature rises its density goes down thus the drag force should be lower and consequently particles should NOT be able of reach the top of vessel, as in enviromental conditions simulation.
What do you suggest about it?. Any idea?
Thanks in advance
|Thread||Thread Starter||Forum||Replies||Last Post|
|Flow meter Design||CD adapco Group Marketing||CD-adapco||3||June 21, 2011 08:33|
|mass flow in is not equal to mass flow out||saii||CFX||2||September 18, 2009 08:07|
|What is the difference between liquid reactive flow and gas reactive flow?||James||Main CFD Forum||6||May 15, 2009 12:14|
|reversed flow at velocity inlet / mass flow inlet||ib||FLUENT||1||March 26, 2007 13:11|
|potential flow vs. Euler flow||curious ...||Main CFD Forum||23||July 21, 2006 07:40|