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Total Pressure problem in a duct

 
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Jul21-12, 07:21 PM   #1
 

Total Pressure problem in a duct


Hello
Please help me, a physical relation which my friend is facing, i'm unable to get my head around..
I created a 2D S-duct, the contours are as follows
1.Static pressure
2.Velocity contours
3. Total pressure gradient graph

intake Velocity 20m/s
Guage pressure is taken as '0' pascals

there is flow separation and reversal at + cruvature
created a rake through the duct to find out the pressure gradient

but the total pressure should be constant in duct, only static pressure changes but i was unable to find out what physical problem is causing such as change as shown in graph

Thanks in Advance
Attached Thumbnails
20-07-2012 18-03-19.png   20-07-2012 18-04-12.png   20-07-2012 18-06-01.jpg  
 
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Jul21-12, 07:22 PM   #2
 
sorry for got to attach geometry, rake view
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20-07-2012 18-02-39.png  
 
Jul21-12, 09:04 PM   #3
 
Inviscid or viscous?
 
Jul22-12, 04:04 AM   #4
 

Total Pressure problem in a duct


viscous, Laminar.

Thanks
 
Jul22-12, 09:15 AM   #5
 
In a viscous flow, total pressure won't be conserved, so it shouldn't have constant total pressure.

I also notice you have a negative static pressure, which makes no sense. That isn't physically possible.
 
Jul22-12, 02:58 PM   #6
 
there is probably an offset used in the CFD code for static pressure, like 101325 Pa. There are good numerical reasons for doing this. 0 Pa would then actually be 101325 Pa.

Also, the Casimir effect can cause negative pressures, but that's quantum physics, so naturally nothing works as it's supposed to.
 
Jul22-12, 03:48 PM   #7
 
The Casimir effect still doesn't cause negative fluid pressures. For starters, it is a quantum electrodynamic effect that occurs canonically in a vacuum. That isn't relevant in the least.
 
Jul22-12, 04:48 PM   #8
 
Yeah as boneh3ad said total pressure isn't conserved in viscus flows. Did you do any hand calculations as a preliminary check of your results? I don't have much CFD experience personally, but it seems strange that the flow separates only at your first curve and not the second.
 
Nov26-12, 12:51 PM   #9
 
ever heard "Pressure Recovery"....

a duct with 98% Pressure recovery is nice....

an "S" duct with a 96% recovery (a length-diameter ratio of say 4'ish) is good too....

if all is perfect... you will loose total pressure from boundary layer effects...

incorporate diffusion and see how messy it gets!! :O
 
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