CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > OpenFOAM > OpenFOAM Running, Solving & CFD

Boundary Conditions for Inlet, OUtlet and Wall/Turbulence Modeling for flow in pipe

Register Blogs Community New Posts Updated Threads Search

Like Tree1Likes
  • 1 Post By danbryan22

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   August 10, 2013, 00:17
Post Boundary Conditions for Inlet, OUtlet and Wall/Turbulence Modeling for flow in pipe
  #1
New Member
 
Daniel Tauro
Join Date: Aug 2013
Posts: 2
Rep Power: 0
danbryan22 is on a distinguished road
Hi Everyone,

I am struggling with the boundary conditions for Inlet/Outlet and Wall for turbulent flow in a pipe using pisoFoam(Parameters- D=0.09m, L=15m, Re=5000) ...I followed the threads which say that the type should be a fixedValue at the Inlet...But still no joy with the simulations....Please help me out..Have been trying to cope with this for the past week....

Regards
ScarFace likes this.
danbryan22 is offline   Reply With Quote

Old   August 10, 2013, 08:44
Default
  #2
Senior Member
 
cfdonline2mohsen's Avatar
 
Mohsen KiaMansouri
Join Date: Jan 2010
Location: CFD Lab
Posts: 118
Rep Power: 16
cfdonline2mohsen is on a distinguished road
Dear Daniel
b.c. for the walls depends on your apporach (high RE or Low Re) which is either wallFunction (for k,Epsilon,R) in High Re or Fixed value (for k&R) (and zero Gradient for Epsilon) in Low Re for turbulent flows. have a look at cfd & turbulent books or search the forum for more info.

If your pipe length is too long you can consider the cyclic B.c.s in inlet&outlet. in this case the channelFoam solver is more suitable because it writes and adds a fixed pressure gradient at each time step. some tools for generating turbulence at inlet had been developed for this case. again search the forums for more info.

But if the length of your pipe is short then the turbulent quantity at the inlet must be specified (k and epsilon) and also the velocity at inlet must be specified.
for outlet zero gradient is a suitable choice for fully developed flow (and of course fixed value for pressure)

You must devote some more time searching in the forum and definitely you can find some more useful threads!
__________________
“If you have an apple and I have an apple and we exchange these apples then you and I will still each have one apple. But if you have an idea and I have an idea and we exchange these ideas, then each of us will have two ideas.”
cfdonline2mohsen is offline   Reply With Quote

Old   August 10, 2013, 13:34
Default
  #3
New Member
 
Daniel Tauro
Join Date: Aug 2013
Posts: 2
Rep Power: 0
danbryan22 is on a distinguished road
Dear Kia

Thanks a lot for the advice...Will definitely check and get back....

Regards
danbryan22 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



All times are GMT -4. The time now is 12:40.