Continue to Site

Eng-Tips is the largest engineering community on the Internet

Intelligent Work Forums for Engineering Professionals

  • Congratulations waross on being selected by the Eng-Tips community for having the most helpful posts in the forums last week. Way to Go!

pressure loss

Status
Not open for further replies.

BlueGlow

Nuclear
Jul 27, 2004
1
I am designing a test loop that will have water flow (~30 gal/min) through a 4 cm pipe with an orifice of about .75 cm. I cannot find any information about approximate pressure drop accross an orifice with such a small diameter ratio. Does anyone have a back of the envelope equation I could approximate this loss (+- 10 psi)? Thanks
 
Replies continue below

Recommended for you

Hi Bluegow

try:

((V2^2-V1^2)^0.5 = (alpha)(2 X g X Htap)^0.5

Permanent Pressure Loss (PPL) = (1- d^2/D^2)

V2 is velocity through orifice in m/s
V1 is velocity down pipe m/s
alpha is the discharge coefficient normally about 0.61 (better values in fluids books)
g is gravitational acceleration 9.8 m/s^2
Htap is the head difference immediately across the orifice in metres of fluid
d is orifice diameter.
D is downstream pipe diameter (infinite for open end so PPL=1 in open end case. Units consistent with d.

So the head loss caused by an orifice in a pipeline is
PPL X Htap

As d/D approaches 1 the results become less accurate.

Cheers

Steve



 
The ISO 5167-1(1995)gives calculations for a dP through an orifice but there is a limitation: d(orifice)>=12,5mm and d/D(pipe)>0,2....0,75. So your rates are slightly out of the range and the estimations will be less precise.
M777182
 
Velocity thru orifice seems to be pretty high. Dependent upon upstream pressure, you might check for cavitation at orifice.
Also, I expect a large delta p. Will thickness of orifice be adequate to take the force created by the pressure drop?
 
Status
Not open for further replies.

Part and Inventory Search

Sponsor