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NPSH-pump suction with compensation loop

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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
 
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I can't visualize this without a big chance for making a stupid guess. Can you save me the potential embarassment and attach a diagram?

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"Pumping accounts for 20% of the world’s energy used by electric motors and 25-50% of the total electrical energy usage in certain industrial facilities."-DOE statistic (Note: Make that 99% for pipeline companies)
 
At least 3.2 There's more, so plus flow resistance of foot valve, the 4 ells around the goosneck plus all the pipe from the bottom of the riser to the pump suction flange. Once the gooseneck fills, then the -3.2 will cancel with the +3.2, but you still have the rest of those NPSH parasites still eating it up.

**********************
"Pumping accounts for 20% of the world’s energy used by electric motors and 25-50% of the total electrical energy usage in certain industrial facilities."-DOE statistic (Note: Make that 99% for pipeline companies)
 
Thanks BigInch. Yes I added friction losses of piping and fittings.

cheers
 
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