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

DPM results same as in converged continuous flow

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   July 29, 2013, 04:58
Default Same results in DPM as in continuous phase
  #1
Member
 
yoooodarulez's Avatar
 
Nick
Join Date: Nov 2009
Posts: 45
Rep Power: 16
yoooodarulez is on a distinguished road
Dear all,

I am having problems calculating the lift and drag coefficients of a s809 wing in a 2phase flowfield (air+rain droplets).I am running the continuous phase first and get both a 1st and a 2nd order convergence.Then i insert the dpm parameters in define>models>dpm and set the wing boundary condition but it seems like im getting the same results as in continuous phase.Any suggestions?Thanks in advance.

Last edited by yoooodarulez; July 30, 2013 at 16:56.
yoooodarulez is offline   Reply With Quote

Old   July 29, 2013, 06:29
Default
  #2
Member
 
yoooodarulez's Avatar
 
Nick
Join Date: Nov 2009
Posts: 45
Rep Power: 16
yoooodarulez is on a distinguished road
My input for DPM is:

-Interaction with continuous phase
-10 continuous phase iterations per DPM iteration
-Unsteady Particle tracking
-Particle Time Step size 0.001
-Number of Time Steps 1
-Max number of Steps 500
-Step Length factor 5
-Spherical drag law
-Droplet breakup/TAB/y0/2 parcels

and for the injections i use a surface type injection released from a plane ahead of my wing in the YZ plane which is releasing inert particles of water liquid with properties namely:

-x vel:the mainstream velocity 29.215
-y vel:the velocity computed from Gunn kinzner equation -3.77327
-diameter:0.0009
-start time 0
-stop time 1000
-total flow rate 0.87645 kg/s (but in here i havent included any area value i have just computed this mumber by multiplying LWC with the mainstream x-velocity)
yoooodarulez is offline   Reply With Quote

Old   July 30, 2013, 13:16
Default
  #3
Member
 
yoooodarulez's Avatar
 
Nick
Join Date: Nov 2009
Posts: 45
Rep Power: 16
yoooodarulez is on a distinguished road
Ok let me pose another question since i figured it out what was wrong anyways.Is there any way to increase the splashed particles apart from introducing more particles?I kept increasing the surfaces from 1 (initially) to 4 surfaces releasing particles and the particles released did increase but the splashed particles came to a limit as it seems.Any suggestions?
yoooodarulez 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
Review: Reversed flow CRT FLUENT 1 May 7, 2018 05:36
DSMC results of low-Mach flow over circular cylinder flotus1 Main CFD Forum 2 November 13, 2012 10:37
Two-phase flow in T-junction, multiphase of DPM? Tony FLUENT 2 July 8, 2008 01:26
fluid flow fundas ram Main CFD Forum 5 June 17, 2000 21:31
computation about flow around a yawed cone Tylor Xie Main CFD Forum 0 June 9, 1999 07:33


All times are GMT -4. The time now is 09:52.