Net positive suction head available calculator

Calculate NPSH available with your own figures.

Your numbers

Use the units shown. Results update as you change valid inputs.

Use NPSH available to compare changes to your inputs. The method and limits below explain the scope.

Examples

Examples

Try the starting example

Absolute free-surface pressure (Pa)
101325
Fluid vapour pressure (Pa)
2339
Surface height above pump datum (m)
2
Suction line head loss (m)
1
Density (kg/m³)
998
NPSH available (m)
11.113991

Try another scenario

Absolute free-surface pressure (Pa)
111457.50000000001
Fluid vapour pressure (Pa)
2339
Surface height above pump datum (m)
2
Suction line head loss (m)
1
Density (kg/m³)
998
NPSH available (m)
12.149289
Calculation method

Calculation method

NPSH available (m)

NPSHa=(pAbs-pVap)/(rho g)+surfaceHeight-headLoss.

Symbols and units
a
Absolute free-surface pressure (Pa)
b
Fluid vapour pressure (Pa)
c
Surface height above pump datum (m)
d
Suction line head loss (m)
e
Density (kg/m³)

Use the units shown. A list keeps the order in which you enter its values. The symbol ^ means “raised to the power of”.

Assumptions & limits

Assumptions & limits

  • Reservoir surface velocity neglected. No required-NPSH/cavitation pass verdict. Supported limits: All required fields must be finite values of the exact declared type and within displayed bounds. Lists contain1–1000 finite numbers. JSON tables are numeric rectangular rows, at most100 rows and30 columns; individual tools have stricter shape/domain constraints. Reservoir surface velocity neglected. No required-NPSH/cavitation pass verdict.
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