|August 26, 2013, 01:18||
Join Date: Feb 2012
Posts: 3Rep Power: 5
I am using multi-phase mixture model.. my fluid are superheated steam(as a primary phase) and water (as a secondary phase). The problem was property of steam(enthalpy) wat i need supposed to get is not getting
(for e.g) For my boundry condition enthalpy value of a steam from a steam table is h=3000kj/kg but wat i am getting from cfd results is nearly h=1200kj/kg...
how to fix the problem ...
Thanks in Advance
Last edited by mari009; August 27, 2013 at 09:56.
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