Calculation method and use
Estimates hydraulic power and approximate motor input from flow, total dynamic head and pump efficiency.

Estimate required hydraulic and motor power from flow rate, total dynamic head and pump/system efficiency.
Calculate hydraulic power, pump shaft power, motor input power and approximate horsepower from flow, total head and efficiencies.
This tool is for preliminary sizing. Final pump selection must also check the pump curve, duty point, NPSH, minimum/maximum flow, motor service factor and manufacturer data.
Estimates hydraulic power and approximate motor input from flow, total dynamic head and pump efficiency.
Total Dynamic Head: the combined static head and system losses the pump must overcome.
Lower efficiency means higher input power for the same hydraulic output.
Approximately 1 kW = 1.341 hp, and 1 hp = 0.746 kW.
Pump sizing is not based on flow and static elevation alone. Static head, pipe friction, minor losses and required discharge pressure combine to form total dynamic head (TDH). CivilCalc connects hydraulic power, pump shaft power and approximate motor input power in one traceable workflow.
Engineering reference updated: 19 September 2026
Shaft and motor input power increase as pump and motor efficiency decrease.
Static elevation difference is not automatically the required pump head. Pipe diameter, length, fittings, flow and terminal pressure all affect the operating point.
Illustrative comparison with TDH = 30 m (98.4 ft), pump efficiency 75% and motor efficiency 90% held constant.
This is not a pump curve. In a real piping system TDH normally changes with flow, so the duty point is found from the intersection of the system curve and pump curve.
| Overall efficiency | Input at 20 L/s, 30 m |
|---|---|
| 80% | 7.36 kW |
| 70% | 8.41 kW |
| 60% | 9.81 kW |
| 50% | 11.77 kW |
No. Add friction, minor losses and any required discharge pressure to establish TDH.
Not directly. Standard motor sizes, pump curves, efficiencies, service conditions and manufacturer data must be checked.
If TDH and efficiency stay constant, yes. In real pipe systems friction rises with flow, so TDH may also increase.
NPSH addresses suction-side cavitation risk and cannot be determined from motor power alone.
It can in variable-demand systems, but savings depend on the system curve and operating profile.