|
[Sponsors] |
October 29, 2012, 08:06 |
heat transfer distribution
|
#1 |
Senior Member
ahmad
Join Date: Feb 2012
Posts: 101
Rep Power: 14 |
I have simulated problem , the base of channel is a heat transfer source ( constant ) , when i plot the total surface heat transfer flux at this section ( the base of the channel ) , its appear as a constant line exept at the end and beginning of the channel ?! i need sombody help me why this happen ??
|
|
October 30, 2012, 00:08 |
|
#2 |
Senior Member
ahmad
Join Date: Feb 2012
Posts: 101
Rep Power: 14 |
can somebody get me some help ??
|
|
October 30, 2012, 01:04 |
|
#3 |
Member
AHMAD
Join Date: Apr 2012
Posts: 54
Rep Power: 0 |
Hi,
What is the type of BC you gave to the base of the channel, is it heat flux or temperature? |
|
October 30, 2012, 01:38 |
|
#4 |
Member
sofia
Join Date: Apr 2010
Location: world
Posts: 31
Rep Power: 16 |
Hi
Is your geometry 2D or 3D |
|
October 30, 2012, 01:40 |
|
#5 |
Senior Member
ahmad
Join Date: Feb 2012
Posts: 101
Rep Power: 14 |
||
October 30, 2012, 01:41 |
|
#6 |
Senior Member
ahmad
Join Date: Feb 2012
Posts: 101
Rep Power: 14 |
||
October 30, 2012, 10:30 |
|
#7 |
Member
AHMAD
Join Date: Apr 2012
Posts: 54
Rep Power: 0 |
As the BC is heat flux, fluent will give you this result(constant heat flux), and if you want to check how the heat flux is changing along the channel base you have to use temperature as BC for the channel base.
|
|
October 30, 2012, 10:32 |
|
#8 |
Senior Member
ahmad
Join Date: Feb 2012
Posts: 101
Rep Power: 14 |
||
October 30, 2012, 10:42 |
|
#9 |
Member
AHMAD
Join Date: Apr 2012
Posts: 54
Rep Power: 0 |
I dont know why fluent give this jump, but have you checked the temperature variation along the channel base, and the heat transfer coefficient. If there isnt any thing wrong so it maybe something related to the nature of the mesh you are using.
|
|
October 30, 2012, 10:46 |
|
#10 |
Senior Member
ahmad
Join Date: Feb 2012
Posts: 101
Rep Power: 14 |
the Tem distribution is ok but the Nu number dont go to standard ( 4.3 ) , Nu go to zero ??
|
|
October 30, 2012, 10:49 |
|
#11 |
Member
AHMAD
Join Date: Apr 2012
Posts: 54
Rep Power: 0 |
could you put a picture of temperature and Nu plots.
|
|
October 30, 2012, 12:34 |
|
#12 |
Senior Member
ahmad
Join Date: Feb 2012
Posts: 101
Rep Power: 14 |
i attached the pictures
|
|
November 3, 2012, 04:52 |
|
#13 |
Member
AHMAD
Join Date: Apr 2012
Posts: 54
Rep Power: 0 |
The temperature of the channel base is decreasing, so Nu number must be increasing along the channel base, but Nu plot doesnt give you this result because of the jump of Nu number at the end of channel, so try to decrease the range of the Y-axis of the plot to see what is the real distribution of Nu number.
|
|
November 5, 2012, 12:21 |
|
#14 | |
Senior Member
ahmad
Join Date: Feb 2012
Posts: 101
Rep Power: 14 |
Quote:
what about Nu no didnt go to 4.32 |
||
November 7, 2012, 12:19 |
|
#15 |
Member
AHMAD
Join Date: Apr 2012
Posts: 54
Rep Power: 0 |
Have you checked the reference values you are using like length and temperature.
|
|
November 7, 2012, 12:21 |
|
#16 |
Senior Member
ahmad
Join Date: Feb 2012
Posts: 101
Rep Power: 14 |
||
March 7, 2013, 01:52 |
|
#17 |
New Member
Matt Carlton
Join Date: Feb 2012
Posts: 2
Rep Power: 0 |
Malay, did you solve your problem with the heat transfer spikes at each end? I am having similar issues. Could it be a problem in the mesh?
|
|
March 7, 2013, 03:06 |
|
#18 |
Senior Member
ahmad
Join Date: Feb 2012
Posts: 101
Rep Power: 14 |
||
March 14, 2013, 23:11 |
Success!
|
#19 |
New Member
Matt Carlton
Join Date: Feb 2012
Posts: 2
Rep Power: 0 |
Malay,
Do you have a constant temperature value set for your inlet total temperature? If so, this may be a problem. For my inlet conditions, I imported a total temperature profile simulating a thermal boundary layer and this fixed the heat transfer spike at the inlet. Best of luck! |
|
March 15, 2013, 03:13 |
|
#20 |
Super Moderator
Alex
Join Date: Jun 2012
Location: Germany
Posts: 3,427
Rep Power: 49 |
Try to untick the "node values" option for your plot.
|
|
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
Inverse and Transient Heat Transfer Problem on commercial software: is it possible? | rogbrito | Main CFD Forum | 1 | February 19, 2019 03:11 |
Quenching simulation : how to set up a conjugate heat transfer between solid&liquid | Rockda | FLUENT | 24 | August 30, 2016 07:33 |
Heat Transfer | ahmed_khatibs | OpenFOAM | 2 | March 20, 2012 05:43 |
Inverse and Transient Heat Transfer Problem on commercial software: is it possible? | rogbrito | CFX | 1 | January 29, 2012 18:48 |
Heat Flux at wall in a conjugate heat transfer problem | Chander | CFX | 2 | July 9, 2011 23:22 |