m2609
Mechanical
- Jun 1, 2012
- 6
I'm trying to find a pump suitable for the below application but having no joy, pump will be offshore and unfortunately it’s on the lowest level of the platform so no chance to increase the NPSHa. Unfortunately we cannot increase the low low level in the vessel so the static head is fixed. Pump will be located very close to the vessel, valves have been minimised and no strainer has been included to ensure we don’t reduce the NPSHa further (fluid is thought to be relatively clean). PD pump is preferred due to the low flow rate, however this will reduce the NPSHa further due to acceleration head loses.
Pumped Fluid: LPG (Dry HC Condensate)
SG: 0.58 to 0.70
Viscosity: 0.2cP
Pumping Temp: Ambient
Flow Rate: 5m3/hr (batch process so flow rate can be changed +/- 25%)
Differential Pressure: 1bar
NPSHa: 0.5m
Any suggestions would be great.
Pumped Fluid: LPG (Dry HC Condensate)
SG: 0.58 to 0.70
Viscosity: 0.2cP
Pumping Temp: Ambient
Flow Rate: 5m3/hr (batch process so flow rate can be changed +/- 25%)
Differential Pressure: 1bar
NPSHa: 0.5m
Any suggestions would be great.