Is My Method for Calculating Pump Head Required Correct?

AI Thread Summary
The discussion focuses on calculating the pump head required for a fluid transfer system involving a pump located 3m above a storage vessel and discharging into a pressurized vessel at 2 bar. The participant has accounted for head losses due to friction and minor losses on both the suction and discharge sides, resulting in a total of 31.345m for the required pump head. The method includes the elevation difference, frictional losses, and the pressure head needed to overcome the pressurized vessel. The calculation appears to be correct based on the provided parameters. The participant seeks confirmation on the accuracy of their approach.
evoke1l1
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Homework Statement


I need to calculate the pump head required for a fluid transfer system.

The pump is located 3m above a storage vessel vented to atmosphere (1 bar) with a total pipe length of 5m to pump suction. The pump discharge is connected to a pressurised vessel at 2 bar absolute with an elevation of 15m and a total pipe length of 27m from pump discharge.

Homework Equations


Fluid Density 960 kg m^3

Head loss from friction on suction side: 0.266m
Minor head losses on suction side: 0.249m

Head loss from friction discharge side: 1.44m
Minor head losses on discharge side: 0.77m

The Attempt at a Solution


I've worked out the head required to overcome the pressurised vessel as:

p/ρg = 100000 / 960 × 9.81 = 10.62m

p = 100000 because this would be the gauge pressure in Pa.

To calculate the pump head required I have basically added the sum of height elevation (18m) plus the minor and frictional losses along with the head required to account for the 1 bar increased pressure of the pressurised vessel. This leaves me with an answer of 31.345m for pump head required (Hp).

Would this method be correct or do I need to re-evaluate my method?
 
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This looks OK to me.
 
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Thank you.
 

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