CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > Siemens > STAR-CCM+

Transitional flow_Heat transfer Issues

Register Blogs Community New Posts Updated Threads Search

View Poll Results: what F means in CFD
Fish 2 13.33%
Fresh 1 6.67%
Free 0 0%
Fluid 12 80.00%
Voters: 15. You may not vote on this poll

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   August 1, 2012, 10:05
Default Transitional flow_Heat transfer Issues
  #1
New Member
 
Giannis
Join Date: Jul 2012
Posts: 5
Rep Power: 13
Giannis is on a distinguished road
Hello Everyone!

I have a strange problem, concerning my CFD project. The project is associated with the flow of a liquid inside a tube whose shape is U (U pipe). At this, I want to examine some temperatures and generally the heat transfer data between the fluid and the pipe. However, my results seem to be far away from what i expected for.
At the following ''wall y+ scene'' you can notice some ''gaps'' at the interface between the fluid and the pipe wall.
I have used k-omega model, since my flow is transitional and I also know that wall y+ value should be less than 1 (y+<1). However, I do not know whether that gaps mean something or are created due to I do not have an appropriate Y+ value. Is it possible to have any other issues with the boundaries? (although i am pretty sure that they are correct).


Any advice would be really helpfull!
Thank you a lot in advance!

Giannis
Attached Files
File Type: docx U pipe_heat transfer.docx (54.8 KB, 19 views)
Giannis is offline   Reply With Quote

Old   August 5, 2012, 10:24
Default
  #2
Senior Member
 
Join Date: Dec 2010
Posts: 135
Rep Power: 15
eRzBeNgEl is on a distinguished road
Could u please give us more information about your mesh setup (prism layers, reference size,..,) and also the mesh report is very interesting
eRzBeNgEl is offline   Reply With Quote

Old   August 5, 2012, 13:33
Default
  #3
New Member
 
Giannis
Join Date: Jul 2012
Posts: 5
Rep Power: 13
Giannis is on a distinguished road
Hello eRzBeNgEl and thank you for your reply!

I noticed that the main problem that I have concerns the quality of the mesh. I used Surface Remesher, Trimmer and Prism Layer properties/models.

I changed the ''Gap Fill Percentage'', ''Minimum Thickness Percentage'' and ''Layer Reduction Percentage'' values, and then I receive somehow better result but still not the excepted one. I also increased the number of prism layers, from 2 (by default value) to 6.
One more problem that I face concerns the computer's power since my geometry is huge (80x6x6 m) and sometimes mesh development is impossible to be implemented.
At this note I would like to ask you sth else if you know about. Is it possible to have any effect if I change the mesh model of the fluid from trimmer to polyhedral, but the pipe's mesh remain trimmer? Currently I have used trimmer model for both fluid and pipe.

Thank you again for your help.

Giannis
Giannis is offline   Reply With Quote

Old   August 6, 2012, 02:47
Default
  #4
Super Moderator
 
flotus1's Avatar
 
Alex
Join Date: Jun 2012
Location: Germany
Posts: 3,399
Rep Power: 46
flotus1 has a spectacular aura aboutflotus1 has a spectacular aura about
Is it really necessary to do a conjugate heat transfer simulation here? In most "flow throug a pipe"-cases, it is not...
That would make the case much easier both in meshing and solving.
flotus1 is offline   Reply With Quote

Old   August 6, 2012, 03:18
Default
  #5
New Member
 
Giannis
Join Date: Jul 2012
Posts: 5
Rep Power: 13
Giannis is on a distinguished road
Hello flotus1!

Actually, I investigate heat transfer phenomena between that geometry and the ground. I work on a Ground Source Heat Pumps problem and I consindered that would be a worth considering approach to investigate many things using CFD.

So the problem is associated with heat transfer, from the fluid to the pipe (convection heat transfer), from the pipe to the (grout - part of Ground Heat Exchangers) and then, from the grout to the ground.
Giannis is offline   Reply With Quote

Old   August 28, 2012, 19:24
Default
  #6
Senior Member
 
Join Date: Oct 2009
Location: Germany
Posts: 636
Rep Power: 21
abdul099 is on a distinguished road
When you really run your case with y+ <1, you need to significantly increase the number of prism layers. About 15 layers is the minimum, while it doesn't harm to have some more.
So I recommend to run with wall functions and 30 < y+ < 150.

With your huge domain, I would use the generalized cylinder mesher when possible or stick to the extruder for straight sections of your pipe. Or when you're using a new version (7.04), you can use directed meshing. It might be a little tricky to get a small, good mesh, but it's worth not just to hit the mesh button using a trimmed mesh.
__________________
We do three types of jobs here:
GOOD, FAST AND CHEAP
You may choose any two!
abdul099 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
problems after decomposing for running alessio.nz OpenFOAM 7 March 5, 2021 04:49
Convective / Conductive Heat Transfer in Hypersonic flows enigma Main CFD Forum 2 November 1, 2009 22:53
How can I increase Heat Transfer at Domain Interf? B.Simon CFX 3 October 28, 2008 18:53
Convective Heat Transfer - Heat Exchanger Mark CFX 6 November 15, 2004 15:55
additional variable mass transfer in CFX5.6 john CFX 1 February 14, 2004 00:30


All times are GMT -4. The time now is 03:23.