rob5377
Chemical
- Oct 3, 2007
- 28
Hi All,
I was asked to review if existing centrifugal pump handle a new suction line arrangement. Pump used to "suck" water 0.7 meters below pump CL and now a compensation loop going 2.5 meters above pump CL was added. My concern is if i should consider 0.7 or (0.7+2,5) meters in static head in calculations. At the begining of suction line foot valve is installed so pipe will be kept flodded. I need it to be sure that in the system is enough NPSHA.
In my opinion during the start up a system will have to overcome 3,2 meters of static head at suction side so I considered this in calculations.
thanks
Rob
I was asked to review if existing centrifugal pump handle a new suction line arrangement. Pump used to "suck" water 0.7 meters below pump CL and now a compensation loop going 2.5 meters above pump CL was added. My concern is if i should consider 0.7 or (0.7+2,5) meters in static head in calculations. At the begining of suction line foot valve is installed so pipe will be kept flodded. I need it to be sure that in the system is enough NPSHA.
In my opinion during the start up a system will have to overcome 3,2 meters of static head at suction side so I considered this in calculations.
thanks
Rob