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

Analysing oil droplet distribution and droplet size of oil in an oil-water mixture

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   March 23, 2022, 11:23
Default Analysing oil droplet distribution and droplet size of oil in an oil-water mixture
  #1
New Member
 
Muhammad Atif
Join Date: Jul 2019
Posts: 4
Rep Power: 7
m.atifme20 is on a distinguished road
Hello all,

I am running an analysis of the oil-water control valves. My aim is to improve the amount of shear generated by the valve body as the flow pass through it. As a result of this shear, the droplet breaks down and the separation of oil from water becomes difficult in the later stage.

I am running oil and water multiphase analysis using the Eulerian model in Ansys Fluent. I am using water as primary and oil as a secondary fluid and I am using sauter mean model to provide range of droplet diameter (min0.0001 to max0.0002). I am new with multiphase and have a couple of questions.

My volume fraction is high and unable to use the DPM model. Is there a way to see droplet size distribution using the Eulerian model?
I used the diameter option available under the properties tab but the information does not make any sense. Please see attached picture, I have created a stratified flow at the inlet where the top half is oil and bottom half of the pipe is water. But the line plot at the middle near the inlet is showing 0.0001 dia of oil whereas this area is completely filled with water(also the contour plot is showing oil droplet at the bottom half of the pipe where it should be zero as the area is covered by water). My question is what is this diameter range and how it is defining the diameter of a droplet when the flow is fully stratified? I used the VOF model as well and the flow pattern at the inlet side was similar but after valve the flow becomes dispersed so the Ansys manual suggests using the Eulerian model. I also have a swirler in the outlet side so the flow would be quite dispersed nature.
I am expecting the oil droplet to break as they pass through the valve and coalescence after passing through swirler. Is it possible to capture this phenomenon without turning the Population balance model ON? I tried turning it on and have not noticed any difference in the results with and without it. The oil volume fraction is high in the middle of the pipe after it passes through the swirler. I am wondering how this coalescence took place when the population balance model was off?
I hope my questions are making sense. Please let me know if something is not very clear here.



Thanks

Muhammad
[ATTACH]Capture1.PNG[/ATTACH]
Attached Images
File Type: png Capture.PNG (24.9 KB, 1 views)
m.atifme20 is offline   Reply With Quote

Reply

Tags
multiphase flow, oil water flow, oil water separator


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
DPM model, droplet size distribution in atomizer model davidx FLUENT 3 May 5, 2017 04:18
Transient water spray in air with droplet distribution as input kar.coep CFX 0 April 14, 2017 10:17
UDF for Droplet size distribution Jufri Fluent Multiphase 1 May 18, 2015 08:27
Plot droplet size distribution curve for Pressure swirl atomizer mali28 FLUENT 1 April 4, 2012 02:27
Initial droplet size distribution Ossi Kaario Siemens 2 March 13, 2001 13:19


All times are GMT -4. The time now is 20:47.