CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > ANSYS > CFX

Some quiestions on multiphase flow

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   June 16, 2009, 14:38
Default Some quiestions on multiphase flow
  #1
New Member
 
Francisca
Join Date: Jun 2009
Posts: 14
Rep Power: 16
fjalil is on a distinguished road
Hi, I'm working on a simulation on multiphase flow. My problem is a launder that carries fluid and particles, and above air, so there are 3 fluids: particles, air, and water. I have some questions on the modeling and I wanted to see if anyone could help. My questions are:

1. For the reference buoyancy density, I don't know if I should use the air density or water density. In the manual it says "For a flow containing a continuous phase and a dilute dispersed phase, you should set the buoyancy reference density to that of the continuous phase", that is, water. On the other hand, it says that for free surface flows, you should use "You should choose the density of the lighter fluid", that is, air. So which one should I use?

2. a) Regarding the fluid details, in the Multiphase Examples section, there is an example of water and sand, where it says to use water as continuous fluid, and sand as dispersed fluid. Why should I use dispersed fluid instead of dispersed solid?

b) In the same section it says that the solid phase should be assigned free slip boundary conditions at walls. To do this and give free slip only to the solid phase (fluid dependent wall influence on flow), I think I must inactivate the homogeneous turbulence option, but on the other hand the manual advices that homogeneous turbulence "is recommended for free surface flow using the inhomogeneous model, separated flow, stratified flow and any situation where the phases tend to separate out". Should I just omit this recommendation?


Thank you very much.

Francisca Jalil V.
fjalil is offline   Reply With Quote

Old   June 16, 2009, 15:58
Default
  #2
Senior Member
 
ckleanth's Avatar
 
George
Join Date: Mar 2009
Location: Birmingham, UK
Posts: 257
Rep Power: 18
ckleanth is on a distinguished road
to model particles in a flow you have two choices. if you chose to use an Eulerian-Eulerian setup then :

1) if you have an Eulerian-Eulerian setup with disperced you should set the buoyancy reference density to that of the continuous phase. if you have two fludis and one disperced use the density of the lighter continious fluid.

2) if you have solid particles use solid disperced but basicaly it depends on your aplication. in order to be able to setup such a model you need to use two fluids. if in your case you have solid particles make a new material and assign solid phase a small insignificant molecular viscosity to it so you can chose the material. The solid phase should be assigned with free slip at walls becasue basicaly its a solid not a fluid and shouldnt "stick" to the walls as fluids do.
use homogenious models unless you have a lot of stirring between phases
__________________
Top 4 tips
1. Knowledge is everything and Ignorance is dangerous.
2. Understand your limitations and try to eliminate them.
3. Get yerself a bike and hoon the chuffer. You will soon learn why dogs like to hang their heads out the car window.
4. Please before asking any questions on how to run simulations in CFX, go though all the tutorials
ckleanth is offline   Reply With Quote

Old   June 16, 2009, 16:29
Default wall influence on flow
  #3
New Member
 
Francisca
Join Date: Jun 2009
Posts: 14
Rep Power: 16
fjalil is on a distinguished road
Thank you very much for your reply. Only one question remains: żis it possible to put fluid dependent wall influence on flow when using homogeneous turbulence models? This option disappears when I mark homogeneous turbulence...so I must put free slip for all the phases and the wall roughness disappears, what can I do if I need wall roughness for the continuous phases (at least for water)?
fjalil is offline   Reply With Quote

Old   June 16, 2009, 18:06
Default
  #4
Senior Member
 
ckleanth's Avatar
 
George
Join Date: Mar 2009
Location: Birmingham, UK
Posts: 257
Rep Power: 18
ckleanth is on a distinguished road
just a tip: when creating the the solid disperced phase, the material thermodynamic state needs to be solid but add the dynamic viscosity value by using cel


it seems that in this case you will need to use fluid dependant turbulence
__________________
Top 4 tips
1. Knowledge is everything and Ignorance is dangerous.
2. Understand your limitations and try to eliminate them.
3. Get yerself a bike and hoon the chuffer. You will soon learn why dogs like to hang their heads out the car window.
4. Please before asking any questions on how to run simulations in CFX, go though all the tutorials
ckleanth is offline   Reply With Quote

Old   June 17, 2009, 12:32
Default Thanks!
  #5
New Member
 
Francisca
Join Date: Jun 2009
Posts: 14
Rep Power: 16
fjalil is on a distinguished road
Thank you!!

Francisca
fjalil is offline   Reply With Quote

Reply

Tags
cfx, cfx11, fluid details, multiphase


Posting Rules
You may not post new threads
You may not post replies
You may not post attachments
You may not edit your posts

BB code is On
Smilies are On
[IMG] code is On
HTML code is Off
Trackbacks are Off
Pingbacks are On
Refbacks are On


Similar Threads
Thread Thread Starter Forum Replies Last Post
Multiphase flow! Amer FLUENT 2 May 16, 2012 15:57
Multiphase flow information amir FLUENT 2 May 25, 2007 06:01
Realizable k-epsilon eqns for multiphase flow Rana FLUENT 0 December 8, 2006 13:46
Multiphase Flow mbga8ejf CFX 0 July 10, 2003 10:26
multiphase flow Shane Gillis FLUENT 10 August 28, 2000 19:12


All times are GMT -4. The time now is 05:36.