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

Boundary condition of velocity inlet

Register Blogs Community New Posts Updated Threads Search

Like Tree2Likes
  • 1 Post By virendra_p
  • 1 Post By virendra_p

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   September 10, 2014, 09:30
Question Boundary condition of velocity inlet
  #1
Member
 
Sa.Baraty
Join Date: Apr 2013
Location: Iran
Posts: 50
Rep Power: 13
sara22 is on a distinguished road
hello guys
i simulate shell&tube heat exchanger in fluent. i use velocity inlet boundary condition. now i question that i must select which options in turbulence part of velocity inlet boundary condition?
K and ep.
intensify and length scale.
intensify and velocity ratio.
intensify and hydraulic diameter.
__________________
thanks
sara22 is offline   Reply With Quote

Old   September 13, 2014, 00:42
Default
  #2
Senior Member
 
A CFD free user's Avatar
 
A-A Azarafza
Join Date: Jan 2013
Posts: 226
Rep Power: 14
A CFD free user is on a distinguished road
It depends on your problem and inlet geometry but in most cases, the third option is more straightforward.
__________________
Regard yours
A CFD free user is offline   Reply With Quote

Old   September 13, 2014, 01:43
Default
  #3
Member
 
Sa.Baraty
Join Date: Apr 2013
Location: Iran
Posts: 50
Rep Power: 13
sara22 is on a distinguished road
tanks about your Ans.
I don't know why mass flow rate at inlet and outlet not be equal?!
this heat exchanger has two fluid domain (Water&Oil).
water: inlet - velocity inlet
outlet - pressure outlet
--------------------------
Oil: inlet - velocity inlet
outlet - pressure outlet
-------------------------------
That this domains are coupled(Thermal condition) together.
for example mass flow rate at inlet and outlet :
water inlet= 1.132
water outlet=0.746
oil inlet=0.171
oil outlet=0.521
__________________
thanks
sara22 is offline   Reply With Quote

Old   September 13, 2014, 14:28
Default
  #4
Member
 
Virendrasingh Pawar
Join Date: Jun 2013
Posts: 47
Rep Power: 12
virendra_p is on a distinguished road
Use intensity and hyd. dia bc. option...you can find empirical relations for I and D involving velocity and geometry data in fluent user guide....just looking at those mass flow rates gives me the impression that water is entering into oil flow domain...some sort of leakage...please check your geometry construction ..... Good luck!
sara22 likes this.
virendra_p is offline   Reply With Quote

Old   September 14, 2014, 01:45
Default
  #5
Member
 
Sa.Baraty
Join Date: Apr 2013
Location: Iran
Posts: 50
Rep Power: 13
sara22 is on a distinguished road
tanks about your ans.
my geometry is ok. i think my mesh file is not suitable.but i cant improve mesh file. its very complex.if possible i send ansys file(project-workbench) for you that you check it.email address please?
__________________
thanks
sara22 is offline   Reply With Quote

Old   September 14, 2014, 02:03
Default
  #6
Member
 
Virendrasingh Pawar
Join Date: Jun 2013
Posts: 47
Rep Power: 12
virendra_p is on a distinguished road
vdp6786@hotmail.com.... I'll have a look
sara22 likes this.
virendra_p is offline   Reply With Quote

Old   September 14, 2014, 10:16
Default
  #7
Member
 
Sa.Baraty
Join Date: Apr 2013
Location: Iran
Posts: 50
Rep Power: 13
sara22 is on a distinguished road
i send project file for you .
thanks about your att.
__________________
thanks
sara22 is offline   Reply With Quote

Old   September 15, 2014, 10:57
Default
  #8
Member
 
Virendrasingh Pawar
Join Date: Jun 2013
Posts: 47
Rep Power: 12
virendra_p is on a distinguished road
Hi....i got the file but unfortunately your ansys is newer so files couldn't be supported by my system...is there any way around?
virendra_p is offline   Reply With Quote

Old   September 15, 2014, 12:44
Default
  #9
Member
 
Sa.Baraty
Join Date: Apr 2013
Location: Iran
Posts: 50
Rep Power: 13
sara22 is on a distinguished road
Thanks. i sent 'stp' file of my model for you
__________________
thanks
sara22 is offline   Reply With Quote

Old   September 18, 2014, 20:14
Default
  #10
Member
 
Virendrasingh Pawar
Join Date: Jun 2013
Posts: 47
Rep Power: 12
virendra_p is on a distinguished road
Hi...i got the geometry....just one doubt...the end where the tube-side fluid (i guess oil in your case) reverses (the semi-sphere at top end)....shouldn't there be plates installed...or else shell-side fluid (water) will intermix...please clear
virendra_p 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
Question about heat transfer coefficient setting for CFX Anna Tian CFX 1 June 16, 2013 06:28
velocity profile inlet boundary condition question Lcw FLUENT 3 August 3, 2012 05:53
Pressure Inlet Boundary Condition Issue zoeburton1987 FLUENT 0 May 15, 2012 09:20
How to set up the inlet boundary condition for a low pressure case? beastieboys6 FLUENT 3 April 10, 2012 22:46
Velocity inlet boundary condition for porous medium Chander CFX 3 March 11, 2012 21:18


All times are GMT -4. The time now is 23:13.