|November 8, 2007, 15:23||
Any body familiar with PBM in Fluent
If you are working on PBM in Fluent and would like to exchange info, please send me a message.
|February 6, 2013, 13:01||
Join Date: Feb 2011
Posts: 12Rep Power: 6
My name is ashar doing my research in Portugal.
I am new to population balance modelling. I am modelling precipitation of barium sulphate
.i.e. (1) Bacl2+ (2) Na2So4------»BaSO4
This study is conducted in T Reactor where two reactant will be fed through the two different inlet and impinge in the center.
Can you please guide me through the problem in order to solve.
Like where should i enter the concentration for example (1) and (2)=0.1.
what will be my Primary phase or Sec Phase. IF i am not wrong I have defined (1) as PP and (2) as SP. or else should i patch the (1) in left side and (2) in right side.
Also in material (1) is not available so therefore I defined water initially then I Changed the Mol. wt. of the component but (2) is available in Fluent database.
Sorry I know I am asking too many questions.
Whatever suggestions you give will be highly appreciated.
|Thread||Thread Starter||Forum||Replies||Last Post|
|6DOF with floating body bounce back.||paka||FLUENT||4||June 6, 2013 11:32|
|Different Results from Fluent 5.5 and Fluent 6.0||Rajeev Kumar Singh||FLUENT||6||December 19, 2010 12:33|
|problem of running parallel Fluent on linux cluster||ivanbuz||FLUENT||11||March 10, 2010 16:13|
|Fluent connection with simulink by TCP/IP||Tanktruck||Fluent UDF and Scheme Programming||1||June 28, 2009 12:56|
|Fluent - license problem.||Marcin||FLUENT||1||March 4, 2005 12:41|