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

Multiphase solid-liquid flow Lagrangian approach

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   June 12, 2020, 17:59
Default Multiphase solid-liquid flow Lagrangian approach
  #1
New Member
 
AJ
Join Date: Feb 2020
Location: United Kingdom
Posts: 20
Rep Power: 6
ajjadhav is on a distinguished road
Hello
I am trying multiphase simulation using a Lagrangian approach. I am using 288 mm stirred tank with baffles and pitch blade impeller.
I use 10 per cent volume of glass beads and 90 per cent water. I inject 1000 glass particle out of 10 per cent and simulate them.
So I have to set the volume fraction of solid particle and water. Since I use 1000 particles out 10 per cent, I can not use 0.1 and 0.9 volume fraction for solid phase and liquid. I can calculate the total volume of 1000 glass beads (v1), but u don't know how to convert that v1 to volume fraction because I don't know the exact volume of the stirred tank, because it includes baffles, shaft, impeller.
So is there any way to get the exact volume of the tank in cfx or how can I set volume fraction of solid particles excluding that 1000 particles.
Or is there any way to set that out of 0.1 volume fraction of solid particle I can use X volume fraction (equivalent to 1000 particle) for injection.
Thank you
Anand

Last edited by ajjadhav; June 14, 2020 at 07:16.
ajjadhav is offline   Reply With Quote

Old   June 13, 2020, 05:46
Default
  #2
Super Moderator
 
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,700
Rep Power: 143
ghorrocks is just really niceghorrocks is just really niceghorrocks is just really niceghorrocks is just really nice
Your question started well, but headed off into XY problem land after a while (http://xyproblem.info/).....

Your problem has nothing to do with the volume of the tank or scaling the volume fraction to account for the 1000 particles. Your problem is you have not read the CFX documentation so you know how lagrangian particle tracking simulations work

In CFX, the tracked particles each represent a large number of particles. Say there is actually 10 million particles in your case, and you are modelling it with 1000 particles. CFX automatically then models those particles so each particle has the effect of 10000 actual particles. So each modelled particle is representative of 10000 actual particles. This means the full volume fraction, interphase drag and other effects are modelled, despite only a fraction of the actual particle number being modelled.

But the most important thing for you to do is to read the CFX documentation. You need to understand a model if you are going to use it.
__________________
Note: I do not answer CFD questions by PM. CFD questions should be posted on the forum.
ghorrocks is offline   Reply With Quote

Reply

Tags
cfx, lagrangian, particle tracking


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
Optimal Settings for two phase(Solid Liquid) granular eularain multiphase flow bhattnaman1 Fluent Multiphase 1 January 31, 2019 21:11
mass flow in is not equal to mass flow out saii CFX 12 March 19, 2018 05:21
Experimental data for a multiphase flow (air and water droplets) with liquid film vaganto Fluent Multiphase 0 December 6, 2016 08:53
Calculating mass flow rate at multiphase flows Kuslo187 OpenFOAM Post-Processing 1 August 21, 2015 18:11
How to visualize the solid body in multiphase flow grid? asoltoon OpenFOAM Post-Processing 2 February 2, 2013 12:40


All times are GMT -4. The time now is 15:54.