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

Need Help in simulating shell and tube heat exchnger

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   August 20, 2012, 07:47
Default Need Help in simulating shell and tube heat exchnger
  #1
New Member
 
Ehsan Akrami
Join Date: Aug 2012
Location: Ireland
Posts: 9
Rep Power: 14
ehsanakrami is on a distinguished road
hi guys . i was simulate a shell and tube heat exchanger . i want calculate reynolds number and heat transfer coefficient(h) , and nusslet number . does Fluent calculate this items directly ? is cell reynolds numb same as reynold number in shell side ?
tnx
ehsanakrami is offline   Reply With Quote

Old   August 24, 2012, 03:42
Default
  #2
Senior Member
 
Ehsan Asgari
Join Date: Apr 2010
Posts: 473
Rep Power: 18
syavash is on a distinguished road
Quote:
Originally Posted by ehsanakrami View Post
hi guys . i was simulate a shell and tube heat exchanger . i want calculate reynolds number and heat transfer coefficient(h) , and nusslet number . does Fluent calculate this items directly ? is cell reynolds numb same as reynold number in shell side ?
tnx

Hi,
Actually Fluent can not calculate these values directly. You should consider some reference parameters in order to get in range results.
Cell Reynolds number is obtained based on Cell mean length and it is not Reynolds number in your case. You need an appropriate reference length for calculating Reynolds number e.g. tube diameter.
Good luck.
syavash is offline   Reply With Quote

Old   August 24, 2012, 03:55
Default
  #3
New Member
 
Ehsan Akrami
Join Date: Aug 2012
Location: Ireland
Posts: 9
Rep Power: 14
ehsanakrami is on a distinguished road
Quote:
Originally Posted by syavash View Post
Hi,
Actually Fluent can not calculate these values directly. You should consider some reference parameters in order to get in range results.
Cell Reynolds number is obtained based on Cell mean length and it is not Reynolds number in your case. You need an appropriate reference length for calculating Reynolds number e.g. tube diameter.
Good luck.
as you now in shell of heat exchanger th diameter is variable and its not a constant value .
ehsanakrami is offline   Reply With Quote

Old   August 24, 2012, 06:40
Default
  #4
Senior Member
 
Ehsan Asgari
Join Date: Apr 2010
Posts: 473
Rep Power: 18
syavash is on a distinguished road
Quote:
Originally Posted by ehsanakrami View Post
as you now in shell of heat exchanger th diameter is variable and its not a constant value .

well, I can't exactly understand what you mean. As I know in shell tube H.E. shell diameter is quite a constant value. I think Inlet air Reynolds number is mostly interested and then you should consider air inlet diameter as reference length for computing Reynolds number.
syavash 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
How to carry out 3D shell and Tube Heat Exchanger analysis in fluent medogalal FLUENT 3 December 30, 2015 05:28
FSI error ERROR #001100279(Shell & Tube heat exchanger) Chandrashekhar CFX 3 March 26, 2010 16:04
3D shell and tube heat exchanger Peter Jansen FLUENT 2 June 7, 2006 08:01
How to simulate 3D shell and Tube heat Exchanger san FLUENT 2 February 22, 2006 06:44
time averaged heat transfer in oscillating flow Matthieu Ubas Main CFD Forum 2 November 5, 1999 15:20


All times are GMT -4. The time now is 15:42.