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

Bondary Discripancy

Register Blogs Members List Search Today's Posts Mark Forums Read

Reply
 
LinkBack Thread Tools Display Modes
Old   February 15, 2002, 04:53
Default Bondary Discripancy
  #1
Theju
Guest
 
Posts: n/a
Hi,

I have specified convective boundary condition on the external surface of a t-pipe with h = 2 btu/hr-ft^2-F and T_infinity = 70 F. But after the solution ,the area weighted average of surface heat transfer co-efficient is 0.02 btu/hr-ft^2-F and when Summary--> bondary conditions were printed it prints 11.34 .. Can any body explain this discrpancy...

Regards Theju
  Reply With Quote

Reply

Thread Tools
Display Modes

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 On
Pingbacks are On
Refbacks are On


Similar Threads
Thread Thread Starter Forum Replies Last Post
temperature inlet bondary condition ypchen FLUENT 2 October 19, 2011 23:36
Runtime changing of bondary conditions evrikon OpenFOAM Running, Solving & CFD 2 November 24, 2009 19:53
dynamic mesh bondary layer cells geri FLUENT 4 October 16, 2007 09:47
How to apply bondary conditions only having mesh. mitul CFX 1 February 10, 2007 04:28
compute bondary layer thickness Ralf Schmidt FLUENT 2 May 31, 2006 07:35


All times are GMT -4. The time now is 15:18.