Gas is being sent from Equipment 1 (Separator) to Equipment 2 (Compressor)
I have a pressure control valve in b/w Eqpment 1 and 2
For line sizing, I have straight line length as 50 feet
I have two ball valves and a control valve (globe valve)
Eqment 1 pressure is 50 psig and control valve is sized for 5 psi pressure drop
Now for line sizing based on equivalent length should I consider the pressure control valve as a globe valve and take equivalent length? OR should I consider equivalent length and also add 5 psi to the overall pressure drop for calculation? What is the suitable approach for line sizing?
For calculating pr. Drop per 100 ft should the pr. Drop across control valve be considered (5 psi)
Sketch Attached
I have a pressure control valve in b/w Eqpment 1 and 2
For line sizing, I have straight line length as 50 feet
I have two ball valves and a control valve (globe valve)
Eqment 1 pressure is 50 psig and control valve is sized for 5 psi pressure drop
Now for line sizing based on equivalent length should I consider the pressure control valve as a globe valve and take equivalent length? OR should I consider equivalent length and also add 5 psi to the overall pressure drop for calculation? What is the suitable approach for line sizing?
For calculating pr. Drop per 100 ft should the pr. Drop across control valve be considered (5 psi)
Sketch Attached