Engineering

Pump Shaft Power Calculator

Calculate pump shaft power with transparent engineering inputs and the displayed formula.

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Engineering screening calculation. Use this as a screening calculation. Verify inputs, material properties, units, governing standards and manufacturer data before final engineering decisions.
Input/output presentation
The calculation remains in its defined base units; supported fields are converted only for display and input.
Fluid & PipingPshaft = ρgQH / η
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Shaft power19.574 kW
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PROFENG provides this tool for engineering screening and educational use. Check the calculation basis, units, physical assumptions, applicable standards, safety factors, equipment data and project-specific requirements before design, procurement or operation.

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Why use this pump shaft power calculator?

Calculate pump shaft power with transparent engineering inputs and the displayed formula. The displayed relationship is Pshaft = ρgQH / η.

Engineering calculation context

What this calculation does

This calculator determines shaft power from fluid density, flow, head, pump efficiency. Use it for preliminary hydraulic screening, sanity checks and transparent comparison of operating cases before detailed equipment or piping design.

SOURCEFLOW / HEADRESULT
Simplified calculation path. It illustrates information flow, not equipment geometry or a construction detail.

Formula and engineering variables

Pshaft = ρgQH / η

VariableDefinitionUnitWorking guidance
rhoFluid densitykg/m³Illustrative screening band: 0 to about 9,980 kg/m³. This is not a design limit.
flowFlowm³/sIllustrative screening band: 0 to about 1 m³/s. This is not a design limit.
headHeadmIllustrative screening band: 0 to about 300 m. This is not a design limit.
etaPump efficiency%Physical screening range: greater than 0% and no more than 100%.

Ranges above are screening guidance or physical bounds where stated. They are not code limits or manufacturer ratings.

Calculated outputs

  • Shaft power (kW): rho*9.80665*flow*head/(eta/100)/1000
Automated verification passed – 30 September 2026 – six numerical cases checked against an independent implementation, with dimensional and monotonicity checks where applicable.

Worked example

  • Fluid density (rho) = 998 kg/m³
  • Flow (flow) = 0.05 m³/s
  • Head (head) = 30 m
  • Pump efficiency (eta) = 75 %
Substitution used for checking(998)*9.80665*(0.05)*(30)/((75)/100)/1000 = 19.574 kWShaft power: 19.574 kW

Assumptions

  • Inputs describe one consistent operating case and use the displayed units.
  • Fluid properties are represented by the entered values and are treated as uniform for the calculation.
  • Steady-state behavior is assumed unless the formula explicitly includes time dependence.

Limitations

  • Transient effects, fittings, compressibility, cavitation margin and manufacturer performance data may require separate treatment.
  • Final piping and rotating-equipment design must use the governing project criteria and applicable codes or standards.
  • Density is treated as constant over the calculation.
  • Flow rate and total developed head refer to the same operating point.
  • Efficiency is expressed as a fraction greater than zero and no more than one.
  • The relationship converts hydraulic power to required shaft power; motor and drive losses are separate unless included in the entered efficiency.
  • The displayed default values are a worked example only; replace them with traceable project or measurement data.

Formula source and acknowledgement

Relationship used: Pshaft = ρ g Q H / η for a pump delivering hydraulic head H at volumetric flow Q with overall pump efficiency η.

The relationship used here follows Igor J. Karassik, Joseph P. Messina, Paul Cooper, Charles C. Heald, Pump Handbook 4th edition (2008), McGraw Hill.

Primary sourceIgor J. Karassik, Joseph P. Messina, Paul Cooper, Charles C. Heald, Pump Handbook 4th edition (2008), McGraw Hill
Secondary cross-checkFrank M. White, Henry Xue, Fluid Mechanics 9th edition (2021), McGraw Hill

Credit for the underlying method belongs to the cited author(s). PROFENG presents its own implementation and wording and is not affiliated with or endorsed by the authors or publishers.

Limits of use for this relationship

  • Density is treated as constant over the calculation.
  • Flow rate and total developed head refer to the same operating point.
  • Efficiency is expressed as a fraction greater than zero and no more than one.
  • The relationship converts hydraulic power to required shaft power; motor and drive losses are separate unless included in the entered efficiency.

Read the PROFENG methodology for formula sourcing and automated checks →

How to use it

Start with the inputs shown above, review the assumptions or options, then generate the result. Where the tool creates a file, keep the original until you have opened and checked the downloaded output.

Frequently asked questions

What does Pump Shaft Power Calculator calculate?

This calculator determines shaft power from fluid density, flow, head, pump efficiency. Use it for preliminary hydraulic screening, sanity checks and transparent comparison of operating cases before detailed equipment or piping design.

What formula does Pump Shaft Power Calculator use?

The calculator uses Pshaft = ρgQH / η. Every input used by the implementation is listed in the variable table on this page.

How is the worked example for Pump Shaft Power Calculator checked?

PROFENG substitutes the displayed default values into the implemented relationship and compares the result against automated verification cases where an independent verifier is available.

What assumptions matter most for Pump Shaft Power Calculator?

Inputs describe one consistent operating case and use the displayed units. Fluid properties are represented by the entered values and are treated as uniform for the calculation. Steady-state behavior is assumed unless the formula explicitly includes time dependence.

Can I use this result for final design or procurement?

Use it as an engineering screening calculation. Final design, procurement, operation or compliance decisions require project-specific data and the applicable engineering method, standard or manufacturer information.

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QUALITY & CORRECTIONS

QA, changelog and corrections

Last QA update: 30 September 2026.

Automated verification passed – 30 September 2026 – six numerical cases checked, with dimensional checks, independent cross-checks for calculators, and unit round-trip checks for converters where applicable.

Changelog

30 September 2026 – source/indexation status, metadata and correction pathway reviewed. Engineering tools display the automated verification label only when they are inside the passing Part 3 verification scope.