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

Puzzling about the "diameter" in Eulerian Model

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   October 19, 2009, 09:38
Default Puzzling about the "diameter" in Eulerian Model
  #1
New Member
 
yuanyuan
Join Date: Oct 2009
Posts: 2
Rep Power: 0
yuanyuan is on a distinguished road
Dear friends,

I am running a simulation for a bubble column. Eulerian Model is adopted into my simulations, where the parameter "diameter of the bubble" need to be specified into the material property. With the different simulations, I am confused by the parameter. My questions are below:

1. Does it stand for the real bubble size in experiments?

2. I think that the bubble size should be a result from the eulerian model, it should be displayed after the simulations, doesn't it? Why we need to specify it before similations?

3. I could get different gas holdups (which is an important parameter for bubble column) with the different "diameters of the bubbles". Furthurmore, it takes a longer time for a simulation coming to a nearly stable result with a smaller "diameter of bubble" . How big should be it?

4. I also have performed simulations with the PBM model. However, I found that a initialization for the bubble size is needed. If I initialized the bubble size with 0.5mm, after calculations, I could find that the maximal number density of the partical diameter is 0.5mm; if I initialized it with 1mm, after calculations, the maximal number density of it is 1mm. Does it indicate that we have to have a prior knowledge about the "diameters of bubbles"?

Thank you very much for explaining,

yuanyuan
yuanyuan is offline   Reply With Quote

Old   October 20, 2009, 22:52
Default
  #2
New Member
 
yuanyuan
Join Date: Oct 2009
Posts: 2
Rep Power: 0
yuanyuan is on a distinguished road
Is there somebody that could help me for the questions above? Thanks again

Quote:
Originally Posted by yuanyuan View Post
Dear friends,

I am running a simulation for a bubble column. Eulerian Model is adopted into my simulations, where the parameter "diameter of the bubble" need to be specified into the material property. With the different simulations, I am confused by the parameter. My questions are below:

1. Does it stand for the real bubble size in experiments?

2. I think that the bubble size should be a result from the eulerian model, it should be displayed after the simulations, doesn't it? Why we need to specify it before similations?

3. I could get different gas holdups (which is an important parameter for bubble column) with the different "diameters of the bubbles". Furthurmore, it takes a longer time for a simulation coming to a nearly stable result with a smaller "diameter of bubble" . How big should be it?

4. I also have performed simulations with the PBM model. However, I found that a initialization for the bubble size is needed. If I initialized the bubble size with 0.5mm, after calculations, I could find that the maximal number density of the partical diameter is 0.5mm; if I initialized it with 1mm, after calculations, the maximal number density of it is 1mm. Does it indicate that we have to have a prior knowledge about the "diameters of bubbles"?

Thank you very much for explaining,

yuanyuan
yuanyuan is offline   Reply With Quote

Old   October 22, 2009, 09:38
Default
  #3
Member
 
JP
Join Date: Mar 2009
Posts: 57
Rep Power: 18
srjp is on a distinguished road
You are right. Eulerian model requires that you know the diameter of the drops / bubbles upfront. It stands for the real bubble size.
You can specify
(1) constant bubble diameter or
(2) The Sauter-mean diameter or
(3) the diameter distribution using a UDF

To model change in diameters due to coalescence, breakup etc, you need "Population Balance Model" which is an add-on module to Fluent. Check if you have it.

Regarding convergence, check your grid size as compared to the bubble diameter. If your diameter is small compared to the grid size, you may run into issues.
srjp is offline   Reply With Quote

Reply

Tags
diameter, eulerial model


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
Superlinear speedup in OpenFOAM 13 msrinath80 OpenFOAM Running, Solving & CFD 18 March 3, 2015 06:36
question about eulerian model for packed bed rone FLUENT 2 July 19, 2007 21:58
Mass and het transfer using eulerian model Pablo FLUENT 0 February 16, 2007 09:36
the Eulerian model and the lower volume fraction hx li FLUENT 2 October 27, 2005 07:17
Strain Rate in eulerian model galeazzo FLUENT 0 January 25, 2005 08:52


All times are GMT -4. The time now is 21:26.