Pump Cavitation Check: NPSH Available vs. Required
Calculate NPSH available for 60 °C water from an open tank at 1,500 m elevation and compare it with NPSH required plus a stated margin.
Mechanical, HVAC & Fluids · Last reviewed
Given
A pump draws water from an open tank at a site 1,500 m above sea level. The water surface is 1.2 m above the pump centerline, and the suction line losses at the design flow are 0.8 m. The water is at 60 °C, with a vapor pressure of 19.94 kPa and a density of 983.2 kg/m³. The manufacturer gives NPSH required = 4.5 m at the duty flow. For this exercise require NPSH available to exceed NPSH required by at least 1.0 m.
Find
NPSH available, and whether the pump is acceptable. Then repeat for 80 °C water.
Solution
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Questions
What happens when NPSHa is too low?
Vapor bubbles form at the impeller inlet and collapse as the pressure recovers. That causes noise, vibration, loss of head and damage to the impeller over time.
Is a 1.0 m margin a standard?
No. It is an exercise value. Margins used in practice depend on the application, the pump type and the owner or standards requirements.
How can I raise NPSHa?
Raise the liquid level, shorten or enlarge the suction line, lower the liquid temperature, or lower the pump.
Educational material. Examples use simplified, hypothetical inputs and are not a design, a construction document or professional engineering advice. Confirm requirements with the codes and standards adopted where the work is built and with a licensed engineer.