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

reversed flow

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   June 28, 2013, 03:51
Default reversed flow
  #1
Member
 
steven
Join Date: Jun 2013
Posts: 41
Rep Power: 12
steven1 is on a distinguished road
hello everyone,

my cas is a 'T' tube connected by two cylindres with an inlet and 2 outlet.
the fluide is turbulent. i made the boundary condition as 'outflow', the warning came to me was "reversed flow". i looked for the former thread, it is said that i could change it to 'pressure outlet'. after operation, the warning is always "reversed flow".
does someone know what happened?

thank you
steven
steven1 is offline   Reply With Quote

Old   June 28, 2013, 06:33
Default
  #2
Super Moderator
 
-mAx-'s Avatar
 
Maxime Perelli
Join Date: Mar 2009
Location: Switzerland
Posts: 3,297
Rep Power: 41
-mAx- will become famous soon enough
you have a vortex crossing the outlet.
It is just a warning, let iterate, the warning may disappear
__________________
In memory of my friend Hervé: CFD engineer & freerider
-mAx- is offline   Reply With Quote

Old   June 28, 2013, 06:36
Default
  #3
azt
Member
 
allan thomson
Join Date: Mar 2009
Location: scotland
Posts: 45
Rep Power: 17
azt is on a distinguished road
Extend your computational domain at the outlets, i.e. ensure that the outlet is far away from the tee
azt is offline   Reply With Quote

Old   June 28, 2013, 07:46
Default
  #4
Member
 
steven
Join Date: Jun 2013
Posts: 41
Rep Power: 12
steven1 is on a distinguished road
Ok, thank you, i will wait a bit.
steven1 is offline   Reply With Quote

Old   June 28, 2013, 07:48
Default
  #5
Member
 
steven
Join Date: Jun 2013
Posts: 41
Rep Power: 12
steven1 is on a distinguished road
Quote:
Originally Posted by azt View Post
Extend your computational domain at the outlets, i.e. ensure that the outlet is far away from the tee
Thank you. in this case the distance of outlets are at least 25 times that of diameter
steven1 is offline   Reply With Quote

Old   June 28, 2013, 07:54
Default
  #6
Member
 
steven
Join Date: Jun 2013
Posts: 41
Rep Power: 12
steven1 is on a distinguished road
Quote:
Originally Posted by -mAx- View Post
you have a vortex crossing the outlet.
It is just a warning, let iterate, the warning may disappear
hello, Maxime,this is what i get. do you have some suggestions?
https://www.dropbox.com/s/30deqc29eq...ed%20flow.docx
steven1 is offline   Reply With Quote

Old   June 28, 2013, 08:44
Default
  #7
Super Moderator
 
-mAx-'s Avatar
 
Maxime Perelli
Join Date: Mar 2009
Location: Switzerland
Posts: 3,297
Rep Power: 41
-mAx- will become famous soon enough
Quote:
Originally Posted by steven1 View Post
hello, Maxime,this is what i get. do you have some suggestions?
https://www.dropbox.com/s/30deqc29eq...ed%20flow.docx
you have a convergence problem, and I don't think it comes to your reversed flow
-check Mesh
-how are your turbulent bc?
__________________
In memory of my friend Hervé: CFD engineer & freerider
-mAx- is offline   Reply With Quote

Old   June 28, 2013, 08:58
Default
  #8
Member
 
steven
Join Date: Jun 2013
Posts: 41
Rep Power: 12
steven1 is on a distinguished road
Quote:
Originally Posted by -mAx- View Post
you have a convergence problem, and I don't think it comes to your reversed flow
-check Mesh
-how are your turbulent bc?
the mesh is not too bad. i chose the standard wall function. here are the informations https://www.dropbox.com/s/30deqc29eq...ed%20flow.docx
steven1 is offline   Reply With Quote

Old   June 28, 2013, 09:19
Default
  #9
Super Moderator
 
-mAx-'s Avatar
 
Maxime Perelli
Join Date: Mar 2009
Location: Switzerland
Posts: 3,297
Rep Power: 41
-mAx- will become famous soon enough
-what is the quality of worst element? (show worst element option in gambit)
-what are the tubulent bc at your inlet (you showed the turbulent model)
-did you scaled your model?
-can you copy and paste the output from checkMesh
__________________
In memory of my friend Hervé: CFD engineer & freerider
-mAx- is offline   Reply With Quote

Old   June 28, 2013, 09:46
Default
  #10
Member
 
steven
Join Date: Jun 2013
Posts: 41
Rep Power: 12
steven1 is on a distinguished road
Quote:
Originally Posted by -mAx- View Post
-what is the quality of worst element? (show worst element option in gambit)
-what are the tubulent bc at your inlet (you showed the turbulent model)
-did you scaled your model?
-can you copy and paste the output from checkMesh
hello, this is the information. thank you
https://www.dropbox.com/s/xml8ctvagskchbf/0628-2.docx


Mesh Quality:
Orthogonal Quality ranges from 0 to 1, where values close to 0 correspond to low quality.
Minimum Orthogonal Quality = 2.75142e-01
Maximum Aspect Ratio = 1.61014e+01
steven1 is offline   Reply With Quote

Old   June 28, 2013, 09:50
Default
  #11
Super Moderator
 
-mAx-'s Avatar
 
Maxime Perelli
Join Date: Mar 2009
Location: Switzerland
Posts: 3,297
Rep Power: 41
-mAx- will become famous soon enough
ok, your mesh is ok and seems to be scaled
in the velocity BC, you should have turbulent parameters, waht do you have?
How is you material? density, viscosity?
__________________
In memory of my friend Hervé: CFD engineer & freerider
-mAx- is offline   Reply With Quote

Old   June 28, 2013, 10:01
Default
  #12
Member
 
steven
Join Date: Jun 2013
Posts: 41
Rep Power: 12
steven1 is on a distinguished road
Quote:
Originally Posted by -mAx- View Post
ok, your mesh is ok and seems to be scaled
in the velocity BC, you should have turbulent parameters, waht do you have?
How is you material? density, viscosity?
i have the parameters of K and epsilon. k=0.053985 and epsilon=1.4722. the velocity is 5m/s, it is calculated with the Re=100000. the material is water-liquid. density is about 1000kg/m3, and viscosity is about 0.001kg/m-s
steven1 is offline   Reply With Quote

Old   June 28, 2013, 10:15
Default
  #13
Super Moderator
 
-mAx-'s Avatar
 
Maxime Perelli
Join Date: Mar 2009
Location: Switzerland
Posts: 3,297
Rep Power: 41
-mAx- will become famous soon enough
Ok I have to hurry
Try to switch with realizable-kepsilon
Try with and without enhanced wall treatment
__________________
In memory of my friend Hervé: CFD engineer & freerider
-mAx- is offline   Reply With Quote

Old   June 28, 2013, 10:21
Default
  #14
Member
 
steven
Join Date: Jun 2013
Posts: 41
Rep Power: 12
steven1 is on a distinguished road
sorry, i didn't understand what you mean 'realizable-kepsilon'. the k,epsilon values that i used are also calculated with Re=100000.
steven1 is offline   Reply With Quote

Old   June 28, 2013, 10:43
Default
  #15
Super Moderator
 
-mAx-'s Avatar
 
Maxime Perelli
Join Date: Mar 2009
Location: Switzerland
Posts: 3,297
Rep Power: 41
-mAx- will become famous soon enough
Quote:
Originally Posted by steven1 View Post
sorry, i didn't understand what you mean 'realizable-kepsilon'. the k,epsilon values that i used are also calculated with Re=100000.
Other turbulence model
__________________
In memory of my friend Hervé: CFD engineer & freerider
-mAx- is offline   Reply With Quote

Old   July 2, 2013, 03:33
Default
  #16
Member
 
steven
Join Date: Jun 2013
Posts: 41
Rep Power: 12
steven1 is on a distinguished road
Quote:
Originally Posted by -mAx- View Post
Other turbulence model
hello Max, i have tried the realizable k-epsilon, but the situation didn't change, there are still problem of conbergence and warnings of reversed flow. By the way, the Y+ is between 5 and 30.
steven1 is offline   Reply With Quote

Old   July 2, 2013, 05:12
Default
  #17
Member
 
rayan
Join Date: Jun 2013
Posts: 65
Rep Power: 12
rayan24 is on a distinguished road
Hi,

I have same problem and I think it is the boundary conditions imposed on your two outputs which poses the problem .. when you have two output can not impose "pressure" at outlet..

What are your boundary conditions at the outlets??



Quote:
Originally Posted by steven1 View Post
hello Max, i have tried the realizable k-epsilon, but the situation didn't change, there are still problem of conbergence and warnings of reversed flow. By the way, the Y+ is between 5 and 30.
rayan24 is offline   Reply With Quote

Old   July 2, 2013, 05:24
Default
  #18
Member
 
steven
Join Date: Jun 2013
Posts: 41
Rep Power: 12
steven1 is on a distinguished road
Quote:
Originally Posted by rayan24 View Post
Hi,

I have same problem and I think it is the boundary conditions imposed on your two outputs which poses the problem .. when you have two output can not impose "pressure" at outlet..

What are your boundary conditions at the outlets??
I use outflow as the BC of outlet. in fact, i had wanted to try the pressure outlet, but i don't know the factors that i have to fill
steven1 is offline   Reply With Quote

Old   July 2, 2013, 08:20
Default
  #19
Member
 
rayan
Join Date: Jun 2013
Posts: 65
Rep Power: 12
rayan24 is on a distinguished road
The condition of pressure outlet is valid when we have "one outlet" for two and more of outlet this condition is not valid, you must use the "equal flow rate" at outlets.. try to reduce the underelaxation at the minimum (0.1 or 0.2)


Quote:
Originally Posted by steven1 View Post
I use outflow as the BC of outlet. in fact, i had wanted to try the pressure outlet, but i don't know the factors that i have to fill
rayan24 is offline   Reply With Quote

Old   July 2, 2013, 08:23
Default
  #20
Member
 
steven
Join Date: Jun 2013
Posts: 41
Rep Power: 12
steven1 is on a distinguished road
Quote:
Originally Posted by rayan24 View Post
The condition of pressure outlet is valid when we have "one outlet" for two and more of outlet this condition is not valid, you must use the "equal flow rate" at outlets.. try to reduce the underelaxation at the minimum (0.1 or 0.2)
so what should I put as the gauge pressure?
steven1 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
Significant Reversed Flow at Outflow Problems [ANSYS FLUENT] NormalVector ANSYS 1 May 15, 2012 23:50
Reversed Flow for a tenth slice of a rotor neptunemmx FLUENT 10 January 30, 2012 13:51
Reversed flow...>>>Please HELP...! sushii FLUENT 14 October 29, 2007 04:27
reversed flow at velocity inlet / mass flow inlet ib FLUENT 1 March 26, 2007 13:11
reversed flow Sastry FLUENT 5 March 22, 2007 08:05


All times are GMT -4. The time now is 17:15.