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Acceleration Head Calculation

05/24/2014 9:47 PM

how to calculate acceleration head,NPSHa,NPSHr of plunger type reciprocating type pumps.

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#1

Re: calculation

05/24/2014 10:35 PM
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#2
In reply to #1

Re: calculation

05/25/2014 2:14 AM

Good but just bear in mind that the OP may work in Imperial gallons which is not the same as US gallons.

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#3
In reply to #2

Re: calculation

05/25/2014 4:00 AM

If the OP is "working" anywhere, they should already know how to do the calculations involved and the units.

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#4
In reply to #1

Re: calculation

05/25/2014 10:52 AM

I can't see anything in that link that tells him how to calculate acceleration head.

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#5
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Re: calculation

05/25/2014 11:30 AM

And?

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#6
In reply to #5

Re: calculation

05/25/2014 1:37 PM

Just that calculation of acceleration head was one of the things OP was asking for help with.

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#7
In reply to #6

Re: calculation

05/25/2014 1:51 PM

Yes, and one would hope that when OP saw how childishly simple it is to get such information by performing a simple search, they would have the gumption and intelligence to find it for themselves.

For OP: Gumption | Define Gumption at Dictionary.com

One can find about 30,800,000 results in 0.25 seconds if one would only take a second to search for the information.

Acceleration Head | Pumps & Systems Magazine

I know that you know this, too bad most who come here don't bother to try it.

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#9
In reply to #7

Re: calculation

05/25/2014 2:20 PM

OK point taken .

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#10
In reply to #9

Re: calculation

05/25/2014 2:37 PM

I applaud your, and other's, willingness to take the time to type out complex explanations to problems for those who are not willing or able to do the work themselves.

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#11
In reply to #10

Re: calculation

05/25/2014 3:23 PM

Thanks. I wasn't going to spoon-feed him on NPSHa, but I thought acceleration head a bit more invoved, though as you point out it's easier enough to find the data.

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#8

Re: calculation

05/25/2014 2:12 PM

Acceleration head is given by

ha = L*V*n*C/K/g

where L = pipe length, V = velocity in pipe, based on nominal flow, n = speed, rpm, C = a constant for the type of pump - no. of cylinders, single or double acting, g = g. Length units what you prefer, as long as you're consistent, time seconds, but n must be rpm. K = a constant, 1.4 for cold water, 2.5 for hot oil, in the paper I'm looking at.

I have a whole list of figures for C for various pump types, let me know which yours is and I'll post.

Above works for suction and discharge, but on discharge can limit L to 15m if actual length is longer, as elasticity in the pipe and compressibility of the fluid mean ha stops increasing after that. But it sounds like you're working on suction, and you'll probably need a pulsation damper. In that case you only need to allow for pipe length between the damper and pump suction. Depending how it works out, you might need a damper on the discharge as well.

NPSHr is not calculated, the figure comes from the pump supplier.

NPSHa is calculated, using acceleration head among other things. There's plenty of data out there.

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