|October 8, 2011, 02:24||
Wet Steam model
Join Date: May 2011
Posts: 22Rep Power: 7
In the multiphase models of FLUENT, Wet Steam model applied for the low pressure flow because the nonisothermal correction factor, θ, given for this flow(low pressure flow). For removing this limitation, I will use the other Source Terms for two additional transport equations and change one or both of them. Iím applicant your guidance, Can you help me?
Last edited by Spring.s; October 8, 2011 at 04:34.
|Thread||Thread Starter||Forum||Replies||Last Post|
|Low-pressure Turbine + Wet Steam||naimishharpal||Main CFD Forum||0||October 5, 2010 16:26|
|mass flow in is not equal to mass flow out||saii||CFX||2||September 18, 2009 08:07|
|2 stage axial turbine model convergence issues||sherifkadry||CFX||2||September 7, 2009 20:51|
|superheated wet steam (avoid condensation in a nozzle)||Ralf Schmidt||FLUENT||0||August 11, 2009 11:55|
|LES and combustion model||Margherita Cadorin||CFX||0||October 29, 2008 06:24|