CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > OpenFOAM > OpenFOAM Running, Solving & CFD

heat transfer convection boundary condition

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   August 8, 2016, 05:06
Default heat transfer convection boundary condition
  #1
New Member
 
Join Date: Jul 2016
Posts: 13
Rep Power: 10
JohnJohn8 is on a distinguished road
Dear all,

I am new to OpenFoam and I want to simulate a block which is cooled by convection at a surface and I am interested in the heat conduction in the block. After research, I found the boundary type: convectiveHeatTransfer, after inputting in as patch type and try to run laplacianFoam I got an error. This error stated that the patch type was unknown. After looking into the source code I saw that the patch type is included in the source code, but only in turbulence sections. Is this patchtype on applicable to turbulent flow settings?

Thanks in advance.

Kind regards

Last edited by JohnJohn8; August 8, 2016 at 06:15. Reason: background of problem
JohnJohn8 is offline   Reply With Quote

Old   August 8, 2016, 11:39
Default
  #2
Senior Member
 
Mahdi Hosseinali
Join Date: Apr 2009
Location: NB, Canada
Posts: 273
Rep Power: 18
anishtain4 is on a distinguished road
As you can see from the patch it's meant for the compressible RAS simulation were it provides the h.
For your case it is q=ha(Tb-Tf), q=kaDT/Dn => kDT/Dn=h(Tb-Tf)
This is a mixed boundary condition. You need to know h.
anishtain4 is offline   Reply With Quote

Old   August 9, 2016, 06:35
Default
  #3
New Member
 
Join Date: Jul 2016
Posts: 13
Rep Power: 10
JohnJohn8 is on a distinguished road
Dear Mahdi,

Thanks for your response.

How exactly do I have to apply this boundary?
Because there is only the thermal diffusivity in the constant folder, how could I specify all the constants?

Thanks in advance.

Kind regards.
JohnJohn8 is offline   Reply With Quote

Old   August 11, 2016, 06:00
Default
  #4
Senior Member
 
Alex
Join Date: Oct 2013
Posts: 337
Rep Power: 22
zfaraday will become famous soon enough
Hi John,

You can check out my web site where I talk about what you need to learn, I think you may find it useful. Besides that, you can also find a further explanation on what Mahdi says in this document, also located in my web.

Hope it helps,

Alex
__________________
Web site where I present my Master's Thesis: foamingtime.wordpress.com

The case I talk about in this site was solved with chtMultiRegionSimpleFoam solver and involves radiation. Some basic tutorials are also resolved step by step in the web. If you are interested in these matters, you are invited to come in!
zfaraday is offline   Reply With Quote

Old   August 11, 2016, 11:48
Default
  #5
Senior Member
 
Mahdi Hosseinali
Join Date: Apr 2009
Location: NB, Canada
Posts: 273
Rep Power: 18
anishtain4 is on a distinguished road
I understand there would be a duplicate of thermal diffusivity, both in constant folder and your boundary condition. But usually this is not that big of a hassle to need to develop your own boundary condition for it. Specially if don't have much experience in OF programming.
anishtain4 is offline   Reply With Quote

Reply

Tags
boundaries condition, heat and mass transfer


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
Centrifugal fan j0hnny CFX 13 October 1, 2019 14:55
Difficulty In Setting Boundary Conditions Moinul Haque CFX 4 November 25, 2014 18:30
Enforce bounds error with heat loss boundary condition at solid walls Chander CFX 2 May 1, 2012 21:11
CFX doesn't continue calculation... mactech001 CFX 6 November 15, 2009 22:25
Natural convection - Inlet boundary condition max91 CFX 1 July 29, 2008 21:28


All times are GMT -4. The time now is 15:10.