CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > OpenFOAM > OpenFOAM Pre-Processing

Outlet with mass flow specified: temperatures diverge

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   April 25, 2016, 09:57
Default Outlet with mass flow specified: temperatures diverge
  #1
New Member
 
Sarah Leenknegt
Join Date: Aug 2015
Posts: 14
Rep Power: 11
SarahLee is on a distinguished road
Dear,

I am trying to run a case with an air curtain at the entrance of a large building, including an outdoor "box" with athmospheric boundaries.
I keep seeing the temperatures at the outlet boundary diverge to unrealistic high values. The meshcheck is successfull, and further refinements have also been made, so I assume the problem is my boundary condition at the outlet. The high temperatures occur at the boundary cells at the outlet area. Already after 20 iterations, the problem starts.

I can post pictures of the geometry with mesh, when required.

The case is running with buoyantboussinesqsimplefoam and kwSST, GAMG solver for p_rgh.

My outlet BDC:
- p = fixedfluxpressure
- p_rgh = fixedfluxpressure
- T = 12 °C (in case of backflow)
- v = x 0; y 1.8; z 0 m/s
- omega = zero gradient
- k = zero gradient
- kappa, alpha, nu = calculated

Important is that I can define the mass flow at the outlet, otherwise the supplied hot air from the air curtain would just flow through the door to outside.

I would appreciate any feedback on potential errors! I have been playing around with different BDC's, but have not found a solution. Or should I look again at my mesh or something else going on with the solver?


In case relevant:

My inlet BDC:
- p = fixedfluxpressure
- p_rgh = fixedfluxpressure
- T = 32 °C
- v = x 0; y 0; z -6 m/s
- omega = turb mix length 0.1 m
- k = turb intensity 5 %
- kappa, alpha, nu = calculated

My athmospheric BDC:
- p = fixedfluxpressure
- p_rgh = totalpressure
- T = -4 °C
- v = pressureinletoutletvelocity
- omega = turb mix length 0.1 m
- k = turb intensity 5 %
- kappa, alpha, nu = calculated

Thanks a lot!

Sarah
SarahLee is offline   Reply With Quote

Old   May 10, 2016, 06:38
Default
  #2
New Member
 
Sarah Leenknegt
Join Date: Aug 2015
Posts: 14
Rep Power: 11
SarahLee is on a distinguished road
In case it can help someone else:

The solution was to set the thermal boundary condition at the outlet to zero gradient.
SarahLee is offline   Reply With Quote

Reply

Tags
buoyanboussinesqsimple, divergence of temperature, outlet bc


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
Plotting mass flow rate at outlet for transient simulation Rakib Fluent Multiphase 4 September 6, 2015 00:46
Mass flow inlet and pressure outlet issue nikhil FLUENT 5 December 11, 2013 13:30
Mass flow rate at the outlet tejasvikrishna FLUENT 2 May 25, 2013 03:42
reversed flow at velocity inlet / mass flow inlet ib FLUENT 1 March 26, 2007 14:11
Mass flow rate in outlet Saturn FLUENT 1 October 11, 2004 10:39


All times are GMT -4. The time now is 19:06.