|
[Sponsors] |
May 19, 2005, 14:07 |
Momentum equation used by mixture model
|
#1 |
Guest
Posts: n/a
|
Hello. I would like to know how FLUENT's momentum equation (eq.24.3-4) for the mixture model was derived. It seems that the 2/3mu term (which is found in the single phase Navier-Stokes equation eq. 9.2-4) has been eliminated in some way, when all the single-phase momentum equations were summed to derive the mixture momentum equation.
I know that the 2/3mu term dissapears when a single-phase flow is incompressible (del dot v =0). However, FLUENT states that one can have multiple compressible liquids in the model. Why then is the 2/3mu term missing from eq. 24.3-4? (I am modelling density currents in reservoirs, driven by suspended sediment. The volumetric concentrations can vary from 1 to say 15%. The mixture model and Discrete phase model appear to be reasonable candidates.) Regards George |
|
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
Question on the discretization of momentum equation in icoFoam | MPJ | OpenFOAM | 3 | October 4, 2011 10:44 |
Derivation of Momentum Equation in Integral Form | Demonwolf | Main CFD Forum | 2 | October 29, 2009 20:53 |
MULTIPHASE - FREE SURFACE & MIXTURE MODEL | Aris | FLUENT | 3 | April 28, 2009 12:46 |
Two-Phase Buoyant Flow Issue | Miguel Baritto | CFX | 4 | August 31, 2006 13:02 |
continuity equation for the mixture | mateus | Main CFD Forum | 0 | May 2, 2003 04:59 |