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

Mixing process

Register Blogs Community New Posts Updated Threads Search

Like Tree1Likes
  • 1 Post By CeesH

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   April 14, 2015, 18:24
Default Mixing process
  #1
New Member
 
P
Join Date: Mar 2015
Posts: 21
Rep Power: 11
paul115 is on a distinguished road
Hello all,

I have the same problem like in this topic but I didn't find solution.
http://www.cfd-online.com/Forums/flu...r-mixture.html

I wanted to model mixing process of 2 fluids in a channel.
Have anyone idea how to resolve this problem ?
At the beginning I had been trying to declerate 2 fluids on 1 inlet . Next I made a baffle on inlet to channel to create 2 inlets and I want to put phase 1 water phase 2 oil and get a mixture at the end of channel. Any idea ?

I will be very grateful for all clues.

Last edited by paul115; April 15, 2015 at 13:18.
paul115 is offline   Reply With Quote

Old   April 15, 2015, 13:19
Default
  #2
New Member
 
P
Join Date: Mar 2015
Posts: 21
Rep Power: 11
paul115 is on a distinguished road
Anyone ? I really need it.
paul115 is offline   Reply With Quote

Old   April 16, 2015, 09:52
Default
  #3
Senior Member
 
Cees Haringa
Join Date: May 2013
Location: Delft
Posts: 607
Rep Power: 0
CeesH is on a distinguished road
Well, I assume you use some multiphase model. For each inlet, under the 'phase-2' tab, you can set under 'multiphase' the volume fraction of phase-2 (and for phase 1, it's 1-phase2 of course). Set them accordingly, that should solve your problem, right?
CeesH is offline   Reply With Quote

Old   April 17, 2015, 05:03
Default
  #4
New Member
 
P
Join Date: Mar 2015
Posts: 21
Rep Power: 11
paul115 is on a distinguished road
Yes. I'm using volume of fluid model. Yes I agree with volume fraction but when I set phase 1 on 1 inlet and phase 2 on 2 inlet I can't even declarate boundary condition. I can declarte them in mixture. Btw I have three options to set: mixture, phase 1 and phase 2. And when I set mixture on 1 inlet and phase 2 on 2nd then I can set volume fraction for 2nd inlet but what about 1 inlet ? I don't what mixture on it. I want phase 1. I don't understand algorithm how to anlyse this case.
I thought I'll be easy. I put phase 1st on 1 inlet phase 2 on 2nd inlet and mixture on output but It doesnt work.
paul115 is offline   Reply With Quote

Old   April 17, 2015, 07:42
Default
  #5
Senior Member
 
Cees Haringa
Join Date: May 2013
Location: Delft
Posts: 607
Rep Power: 0
CeesH is on a distinguished road
I have a bit of a hard time understanding what you mean. Could you provide an image of the mesh? I do assume that inlet 2 and inlet 1 are different boundaries?

Regarding the options: you have to set parameters for each phase and the mixture, even if pure phase-1 or phase-2 flows in. Wheter pure-1 or pure-2, or a bit of both flow in depends on the value you set for phase-2-multiphase

Best,
Cees
CeesH is offline   Reply With Quote

Old   April 20, 2015, 07:08
Default
  #6
New Member
 
P
Join Date: Mar 2015
Posts: 21
Rep Power: 11
paul115 is on a distinguished road
First of all, I am really grateful for your help.

So should I declarate inlet1 mixture and inlet2 phase 2 and set volume fraction 0,5 if I want to have for example 50% water and 50% oil ? And what about backflow volume fraction on outlet ? It also should be 0,5 ?
paul115 is offline   Reply With Quote

Old   April 20, 2015, 08:48
Default
  #7
Senior Member
 
Cees Haringa
Join Date: May 2013
Location: Delft
Posts: 607
Rep Power: 0
CeesH is on a distinguished road
Well, in essence, both inlets are always declared as a mixture. As soon as you use multiphase, every cell contains a mixture of all phases. Only in some cases the mixture contains 100% or 0% A. For computational purposes, it's still a mixture though.

Indeed you are right, if you want the inlet to be 50-50, set the volume fraction to 0.5. A volume fraction of 1 gives pure phase 2, of 0 gives pure phase 1.

backflow should be set at all outlets; in case there is a negative flowrate through part of the outlet (which can happen, for example if the operating pressure is higher than the pressure close to part of the outlet) then the outlet will turn into an inlet - and an inlet boundary needs a volume fraction.

This fraction should be determined based on what you know about the system. If you have only 1 outlet, the calculation is easy. If you have multiple outlets, make an educated guess: for example if one outlet should transport only oil, set the backflow to only oil.
paul115 likes this.
CeesH is offline   Reply With Quote

Old   April 20, 2015, 10:33
Default
  #8
New Member
 
P
Join Date: Mar 2015
Posts: 21
Rep Power: 11
paul115 is on a distinguished road
Thank you very much. You really made me to understand a problem
paul115 is offline   Reply With Quote

Old   April 20, 2015, 10:48
Default
  #9
Senior Member
 
Cees Haringa
Join Date: May 2013
Location: Delft
Posts: 607
Rep Power: 0
CeesH is on a distinguished road
You're welcome!
CeesH is offline   Reply With Quote

Old   May 8, 2015, 06:04
Default
  #10
New Member
 
P
Join Date: Mar 2015
Posts: 21
Rep Power: 11
paul115 is on a distinguished road
Hello all,


I have question to density scale. I'm giving on 1 inlet fluid density 790 on the 2nd 889 and when I get results it looks like on the 1st inlet was 835 density instead of 790 and there isn't any sign of 790 density. Why ? I'm trying to mix 2 fluids and it looks like 2 separate objects in the pipe. There isn't any interaction between 2 fluids.
Maybe I should turn on an extra option or sth like that ?

Please help me. I will appreciate all clues.

P.S I marked on screen what I am wrtiting about
Attached Images
File Type: jpg density.jpg (49.0 KB, 19 views)

Last edited by paul115; May 8, 2015 at 11:04.
paul115 is offline   Reply With Quote

Old   May 9, 2015, 08:14
Default
  #11
New Member
 
P
Join Date: Mar 2015
Posts: 21
Rep Power: 11
paul115 is on a distinguished road
Anyone I really need to solve that problem but I don't have an idea
paul115 is offline   Reply With Quote

Old   September 3, 2015, 17:39
Default
  #12
New Member
 
Join Date: Aug 2015
Posts: 5
Rep Power: 11
Karu_p is on a distinguished road
Paul could you able to solve the mixing problem. I have been working on the same thing for the last week. Anyway VOF is not correct for mixing purpose. DO reply me if you done it.

Thanks in advance
Karu_p is offline   Reply With Quote

Reply


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
The fl process could not be started because of UDF majid_kamyab Fluent UDF and Scheme Programming 6 December 15, 2015 09:42
What's is mixing law richard ben FLUENT 4 September 25, 2014 18:30
error 262144 and unexpected disconnect when run on 2 nodes Emily1412 SU2 Installation 1 April 10, 2014 18:08
Meshing a Mixing Plane using ICEM Will Anderson FLUENT 0 November 6, 2010 18:08
Mixing plane geometry definition Hbet FLUENT 0 January 18, 2002 08:16


All times are GMT -4. The time now is 18:36.