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

Euler model

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   November 13, 2002, 10:03
Default Euler model
  #1
Bharath
Guest
 
Posts: n/a
Hello Is Euler-Euler model ..a better way to model nozzle spray ?? or do we have any restrictions in it ? If someone finds an example or tutorial other than fluent to model Spray ..please provide me with the info.

Thanks

Bharath
  Reply With Quote

Old   November 13, 2002, 20:17
Default Re: Euler model
  #2
Jin-Wook LEE
Guest
 
Posts: n/a
As a my personal point of view, in general, DPM is better than spray model. However, mass flow rate of droplet(or particle) is very high, E-E model is preferred.

Let droplet mass flow rate, D, and gas mass flow rate, G.

In general,

D/G < 0.2, DPM without interaction between two phases.

D/G > 0.2, DPM with interaction between two phases.

The limitation of DPM is the ratio of volume flow rate, D_vol/G_vol about 0.1(10%)~0.15(15%). My personal experience, the ratio of mass flow rate, D/G exceeds 2~3, convergence has some problem.

So, E-E model is recommended for D/G >> 1.

Sincerely, Jinwook

  Reply With Quote

Old   November 14, 2002, 10:21
Default Re: Euler model
  #3
Bharath
Guest
 
Posts: n/a
Hello there Thanks for the reply.However,my problem includes inlet condition of water(as a continous medium ) and air mixing .DPM model would require liquid ( water) phase to be injected as Particles isnt it ??I would like to send the inlet Liquid not as particle but as a continuous flow until the air interacts with it and by its shear force forms droplets. I did find that ..If I use DPM model ,Im able to track only finite number of particles (which is equal to the GRID size at the liquid phase inlet ). But it is required that I wanna see water slowly disintegrating to form droplets and ...not like tracing the Water particles from the very beginning !

Awaiting ur reply

Thanks

Bharath
  Reply With Quote

Old   November 14, 2002, 22:46
Default Re: Euler model
  #4
Jin-Wook LEE
Guest
 
Posts: n/a
Then, it is very difficult(actually, impossible) to solve your problem by E-E model of current Fluent version.

Instead, Fluent has couple of special models for the prediction of droplet formation in DPM option of Fluent 6.0 or higher. I never tried one of these models but I felt that it's very nice.

Sincerely, Jinwook

  Reply With Quote

Old   November 24, 2002, 01:18
Default Re: Euler model
  #5
mahdi saniee nezhad
Guest
 
Posts: n/a
Dear sir I have a problem with this title. If it's possible for you please send me your received responses. Very thanks for your attention to my request. With the best regards. Mahdi saniee nezhad

  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
multiphaseInterFoam for RAS turbulence model chiven OpenFOAM Bugs 8 December 6, 2017 02:08
Superlinear speedup in OpenFOAM 13 msrinath80 OpenFOAM Running, Solving & CFD 18 March 3, 2015 05:36
MRF and Euler model DropsandSimulations OpenFOAM Running, Solving & CFD 0 September 4, 2009 05:20
multi fluid mixture model issue rystokes CFX 3 August 9, 2009 19:13
Advanced Turbulence Modeling in Fluent, Realizable k-epsilon Model Jonas Larsson FLUENT 5 March 13, 2000 03:27


All times are GMT -4. The time now is 01:02.