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

pressure-swirl atomizer spray simulation

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   September 24, 2012, 11:20
Default pressure-swirl atomizer spray simulation
  #1
Member
 
leo
Join Date: Jun 2012
Posts: 98
Rep Power: 14
sjtusyc is on a distinguished road
Before i do this simulation, i have done some literate work and figured out how to do post analysis.
Because i want to do a simulation with time dependent BC, i chose to use CFX which has powerful CEL.

But i have'n't found anybody do pressure-swirl atomizer spray simulation. So
it is tricky.

Up to now, i have some questions.
For my simulation,PTM model with main-break up and second beak up model is the obvious option.

And think the settings of the drag model/main-break up model/second beak up model is most important.

But there are so much sub-settings that it seems impossible to do all the sensitivity analysis. And some of the model is so complex that i can't understand related settings?

How can i effectively handle these settings. any advice ,thank you.

Last edited by sjtusyc; September 24, 2012 at 11:35.
sjtusyc is offline   Reply With Quote

Old   September 24, 2012, 23:02
Default
  #2
Super Moderator
 
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,871
Rep Power: 144
ghorrocks is just really niceghorrocks is just really niceghorrocks is just really niceghorrocks is just really nice
What are you trying to get out of this model? I do not understand what sort of results you are looking for.
ghorrocks is offline   Reply With Quote

Old   September 24, 2012, 23:26
Default
  #3
Member
 
leo
Join Date: Jun 2012
Posts: 98
Rep Power: 14
sjtusyc is on a distinguished road
It is a spray simulation.
I wanna to get SMD and the particle diameter distribution.
sjtusyc is offline   Reply With Quote

Old   September 25, 2012, 09:06
Default
  #4
Super Moderator
 
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,871
Rep Power: 144
ghorrocks is just really niceghorrocks is just really niceghorrocks is just really niceghorrocks is just really nice
Are you happy to get the droplet diameters from models like LISA?

Quote:
But there are so much sub-settings that it seems impossible to do all the sensitivity analysis. And some of the model is so complex that i can't understand related settings?
Nobody said CFD was meant to be easy. Your best chance to do a good simulation is to do a good literature study to start off and find out how the models work and how other people have applied them. Then you will know what is important.
ghorrocks is offline   Reply With Quote

Old   September 25, 2012, 23:50
Default
  #5
Member
 
leo
Join Date: Jun 2012
Posts: 98
Rep Power: 14
sjtusyc is on a distinguished road
Quote:
Originally Posted by ghorrocks View Post
Are you happy to get the droplet diameters from models like LISA?



Nobody said CFD was meant to be easy. Your best chance to do a good simulation is to do a good literature study to start off and find out how the models work and how other people have applied them. Then you will know what is important.
Yes, i wanna to use LISA model as main break-up model,not good?
I did some literature work and will go on doing and find out how the models work and how other people have applied them.

Last edited by sjtusyc; September 26, 2012 at 01:23.
sjtusyc is offline   Reply With Quote

Old   September 26, 2012, 09:10
Default
  #6
Super Moderator
 
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,871
Rep Power: 144
ghorrocks is just really niceghorrocks is just really niceghorrocks is just really niceghorrocks is just really nice
LISA is fine, I just wanted to know whether you wanted to use a breakup model (eg LISA) or if you wanted to directly model the breakup process with a free surface model. So in your case it seems the breakup model is what you want.

There is a lot of literature on LISA and other spray breakup models. They should give you some idea of how to drive them.
ghorrocks is offline   Reply With Quote

Old   September 26, 2012, 23:37
Default
  #7
Member
 
leo
Join Date: Jun 2012
Posts: 98
Rep Power: 14
sjtusyc is on a distinguished road
Thank you.
I am clear about what model should i use, but not clear about the related sub settings.
Next week is Mid-Autumn Festival and National Day, i have a week holiday.
I will do some literature work at home before i come back to school
sjtusyc is offline   Reply With Quote

Old   September 27, 2012, 08:43
Default
  #8
Super Moderator
 
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,871
Rep Power: 144
ghorrocks is just really niceghorrocks is just really niceghorrocks is just really niceghorrocks is just really nice
Yes, the literature is always the starting point when you are doing a new simulation.
ghorrocks 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
Pressure Inlet VS velocity Inlet difference Mohsin FLUENT 9 January 4, 2021 11:34
Pressure Outlet Guage pressure Mohsin FLUENT 36 April 29, 2016 18:16
droplet size distrubution for pressure swirl atomizer niket shah FLUENT 0 April 4, 2012 03:08
stagnation pressure in transient flow simulation K.S.Ravichandran Main CFD Forum 2 September 5, 2000 01:34
Hydrostatic pressure in 2-phase flow modeling (long) DS & HB Main CFD Forum 0 January 8, 2000 16:00


All times are GMT -4. The time now is 17:00.