|December 6, 2004, 07:38||
Transport modelling of concentration in ponds
I am trying to model the transport of rhodamine concetration in waste stabilisation ponds. I have used the "user defined scalar" and have included the convective term. My inlet boundary conditions are inlet velocity and specified scalar value of 1.
Outlet boundary conditions are pressure outlet of 0 value with scalar value of 0. I have not included the source term.
The results are not what I am expecting. Can anyone help how I can overcome my problem.
|Thread||Thread Starter||Forum||Replies||Last Post|
|Modelling Biomass Combustion via Species Transport||Racheal||FLUENT||28||March 4, 2014 23:22|
|UDF for concentration transport equation||heri||FLUENT||1||August 15, 2011 11:23|
|free oil spill transport modelling software||Daniela & Delia||Main CFD Forum||1||June 25, 2004 12:18|
|Concentration modelling||Peter||CD-adapco||1||September 8, 2003 03:22|
|modelling tracer as UDS: too slow transport||Bob||FLUENT||0||March 12, 2003 13:25|