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

Questions on a pressure profile

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   March 28, 2013, 17:53
Default Questions on a pressure profile
  #1
Senior Member
 
---------
Join Date: Oct 2010
Posts: 303
Rep Power: 18
saisanthoshm88 is on a distinguished road
I have some questions on a pressure profile obtained from a simple 2D laminar pipe flow.

Please look into the attached .jpg image of the pressure contour

Could some one please provide clarifications to the following questions I have -

As the flow proceeds from the inlet, there is a gradual pressure drop. Could this be solely attributed to the frictional losses due to wall shear ?

The bernoullis theorem doesn’t seem to hold good here because it is expected that the pressure should increase as the cross sectional area increases for the flow, however a pressure drop is witnessed from the plot. Could you please explain the limitation of bernoullis theorem in this case
Attached Images
File Type: jpg 2DPipeFlow.jpg (57.9 KB, 13 views)
__________________
Best regards,
Santhosh.
saisanthoshm88 is offline   Reply With Quote

Old   March 29, 2013, 05:47
Default
  #2
Member
 
Benny
Join Date: Apr 2012
Posts: 40
Rep Power: 14
Benfa is on a distinguished road
Bernouli says that the "total pressure" is concerved for a streamline. But because of frictional losses etc the tot pressure does not stay const. Total pressure consist out of a dynamic pressure an the static pressure. If you get an increase in flow x-section the "static pressure" will increase.
Benfa is offline   Reply With Quote

Old   March 29, 2013, 05:58
Default
  #3
Senior Member
 
---------
Join Date: Oct 2010
Posts: 303
Rep Power: 18
saisanthoshm88 is on a distinguished road
Thank you very much for your response. I've gone through some books and found that it's a case of Poiseuille flow. Bernoullis theorem is not applicable here as it is a viscous flow (the flow has a very low reynolds number so the viscous effects dominate the inertia). Yes the pressure drop is due to the viscous shear , the shear stress acts in a direction opposite to the flow and a pressure drop from inlet to outlet is required to counter balance this.
__________________
Best regards,
Santhosh.
saisanthoshm88 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
"Pressure Inlet" Boundary Setup Wijaya FLUENT 15 May 18, 2016 11:08
Two fundamental questions about icoFoam while updating the velocities and pressure dbxmcf OpenFOAM Running, Solving & CFD 6 April 12, 2016 17:05
Few simple questions concerning boundary conditions (pressure) milos OpenFOAM Pre-Processing 1 March 21, 2009 08:08
Neumann pressure BC and velocity field Antech Main CFD Forum 0 April 25, 2006 03:15
Hydrostatic pressure in 2-phase flow modeling (long) DS & HB Main CFD Forum 0 January 8, 2000 16:00


All times are GMT -4. The time now is 22:03.