Dear Friends,
I need to know whether I calculate the required brake horsepower for a duplex plunger pump in a correct way or not.
We want to purchase a plunger pump with following operating conditions:
Handled liquid: steam condensate
Operating temperature: 38°C
Discharge pressure: 63 bar
Suction pressure: 0 bar
Normal Capacity at operating temperature: 3.44 m3/hr
Specific Gravity: 0.993
Viscosity (cP): 0.68
Moreover, it is possible that we work with the capacity about 3.9 m3/hr for a short period of time.
Based on API 675 (2.1.15) I calculate the rated capacity 10% greater than Maximum capacity which is 3.9*1.1= 4.29 m3/hr.
I calculate the BHP of PD pump based on 85% efficiency and rated capacity, the equation is Q×ΔP/η. The estimated required BHP is 4.29*63*100000/(3600*0.85)=8.83 kW.
Am I right!?
It would be grateful if you could help me.