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

influence of porous zone in particel resistance time using Euler-Lagrange and DPM ?!

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   April 23, 2010, 06:07
Default influence of porous zone in particel resistance time using Euler-Lagrange and DPM ?!
  #1
Member
 
Roman Gobitz-Pfeifer
Join Date: Dec 2009
Location: Stuttgart
Posts: 83
Rep Power: 16
Wikie is on a distinguished road
Hello,

I'm trying to simulate the evaporation of water droplets. The droplets are injected at the top and should run through a structured packing (2D). I'm using a porous zone to simulate the structured packing and DPM to simulate the droplets. Due to heat and mass transfer, a natural convection should flow through the packing from the bottom to the top. Every thing is working fine in a physical point of view, except the particle resistance time. It's to less. Based on experimental results, the droplets should need 20 sec to flow through the packing (height: 80cm). Now the resistance time is just 0.4 sec. Due to this the mass and temperature change of the discrete phase and of the (humid) air flow is to less.
Doesn't FLUENT include the porous zone into the calculation for the DPM?? If so, how can I include this manually??
Any other suggestions the solve this problem??

cheers
wikie

Last edited by Wikie; April 23, 2010 at 08:05.
Wikie 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



All times are GMT -4. The time now is 00:33.