Calculating Orifice Profile and Plate Thickness for 48" Pipeline

AI Thread Summary
The discussion focuses on calculating the orifice profile and plate thickness for a 48" pipeline with air as the medium, operating under specific pressure conditions. The target pig speed is 0.5 m/s, with upstream pressure at 17 barg and downstream at 0.2 barg, indicating critical flow conditions. Participants discuss the formula for calculating the speed of sound in the pipeline and the resulting volumetric flow to determine the orifice area. One user estimates an orifice diameter of approximately 63 mm using a discharge coefficient (Cd) of 0.8, while another suggests that a Cd of 0.6 may be more accurate. Accurate calculations are essential for effective pig speed control in the pipeline.
badri2221
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We have a situation where we have air in front of the dry pigs and need to control the pig speed

Medium is air, pressure is 17 barg upstream and 0.2 barg downstream and pig speed target is O.5 m/s for the pig in the 48" pipeline with a pressure of 17 barg.

need to find the following:

Orifice profile (hole) size?
Plate thickness
 
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For these upstream and downstream conditions the flow is critical, sonic, or "choked" which means the velocity is limited by the speed of sound in the orifice throat.

So a quick estimate is to calculate the speed of sound in the pipeline:

v_sonic = sqrt (k R Tstar)

k = isentropic exponent
R = gas constant
Tstar = 0.8333 Tgas

The volumetric flow is:

V_flow = v_sonic * A_orifice

and solve for A_orifice which is the area of the orifice. Then you can find the orifice bore size from this area.
 
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thanks , i have tried to model it on massflow and Cd as 0.8 landed around 63 mm dia
 
badri2221 said:
thanks , i have tried to model it on massflow and Cd as 0.8 landed around 63 mm dia

Glad to hear you have this running. I think CD of .6 is closer for an orifice.
 
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