|October 8, 2012, 13:08||
Join Date: Aug 2012
Posts: 14Rep Power: 6
I have already posted in forum regarding my problem. The link is as mentioned below
Species transport and reaction
I want to simulate the reaction between Li and SF6 to find out the temperature profile in the reactor at different times. The reactant "Li" is already present in the enclosed reactor and "SF6" is injected through a nozzle. My problem is how do I input in FLUENT that a certain amount say 2kg of Li is already present in the reactor.
I tried using the patch option in initialize...I patched Lithium to the interior...but the patch option for species is in mass fraction..when I patch the interior with Li mass fraction of 1 and take the volume integral of species mass fraction I get the total mass of lithium to be 5grams...
Is the approach that I am using correct ? Can I give mass fraction in patch greater than 1 (though technically seems incorrect) ??
|Thread||Thread Starter||Forum||Replies||Last Post|
|Heterogeneous reaction between phases with VOF model||sooroo3||Fluent UDF and Scheme Programming||0||February 15, 2011 03:59|
|Segmentation fault in running alternateSteadyReactingFoam,why?||NewKid||OpenFOAM||18||January 20, 2011 17:55|
|multiphase heterogeneous reaction definition||coalgas||FLUENT||0||February 9, 2010 03:05|
|Surface Reaction Model or Heterogeneous Rxn Model?||satheeskannan||FLUENT||0||September 2, 2008 18:55|
|chemical reaction - decompostition||La S. Hyuck||CFX||1||May 23, 2001 00:07|