In a situation a Progressive Cavity pump is selected for handling hydrocarbon and produced water @ 16m3/hr (rated cap), 0.6 barg (suction pressure) and 2.4 barg (discharge pressure).
The NPSHA = 1m.
Design suction pressure = 13.6 barg
Design discharge pressure = 17 barg
The recommended relief setting at discharge = 17barg is based on discharge design pressure.
As per API 676, a PSV shall not be set according to casing/piping design pressure but according to max operating pressure of the pump. The correct PSV setting as per API 676 would be maximum operating pump discharge pressure +1.7 bar.
The above will lead to oversizing of pump as it has to handle the design pressure.
Points for discussion -
(1) In case of suction reaching to its design case i.e. 13.6barg in case of emergency, will that be transferred to discharge even in case of a PC pump?
(2) What way will the pump deliver at suction design pressure, if we want it not to trip before relief setting?
(3) Any alternative suggestion for this situation?