NPSHA is calculated using the following equation:
NPSHA = Hp - Hvap + Hst - Hsf
where:
| Hp | absolute system pressure at the surface of the liquid supply |
| Hvap | vapor pressure of the liquid at the pumping temperature |
| Hst | static height difference between the liquid supply surface and the established pump datum (usually the height of the pump impeller center line) |
| Hsf | all suction line losses including entrance losses, friction losses, valves, fittings etc. |
all expressed in terms of liquid head at the pumping temperature (in meters)