|July 19, 2011, 02:30||
Volume fraction of dispersed phase to determine DPM, VOF, Mixture model
Join Date: Mar 2010
Location: South Korea
Posts: 249Rep Power: 9
For using DPM model in fluent, volume fraction of disperesed phase should be below 10% to 12 %, otherwise you have to look for other models such as mixture and VOF models in fluent.
For determining Volume fraction of a particle, the following formula is used:
where alpha= volume fraction of solid phase
Np=Number of particles
Vp=Volume of particle
Vc= Volume of the container or total volume of the cylinder or the whole control volume.
If alpha comes out to be greater than 12% then "mixture" or "VOF model" would be considered for dense phase.
Please comment if the above statements are correct/wrong.
Thank you so much.
|July 19, 2011, 03:29||
Join Date: May 2009
Location: Montreal, QC
Blog Entries: 1Rep Power: 15
The whole idea is right but some other points should be noted:
- Actually this range is not very tight; it's just a rule of thumb, I believe that if Lagrangian modeling could be proper for a case we can use it.
- Note that DPM modeling in FLUENT encounter many bugs in brownian motion and computing deposition, so in many cases in which diffusion term is dominant in dispersion; such as nano-particles, we have to use eulerian modeling, i.e. solving a transport eq. to find particle concentration.
|January 30, 2015, 13:47||
Join Date: May 2011
Posts: 231Rep Power: 8
I am simulating gas-solid flow with two fluid approach with fluent and I am trying to have 20% mass loading of the particle at the inlet.
as it is same inlet for both phases area is not important...
my air density is 1.2 kg/m3, velocity is 9.3 m/s.
solid density is 2500 kg/m3 , I think velocity must be calculated but I am not sure or I can use 9.3 for solid as well?
how I can calculate the uniform volume fraction of the solid at inlet while assuming constant particle to gas velocity ratio?
do you have any idea?
thanks in advance!
|June 7, 2016, 02:52||
how to define volume fraction in dpm
Join Date: Jun 2016
Posts: 2Rep Power: 0
i have slurry jet (water and sediment).i cant define volume fraction for this problem.i define injection from surface.....
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