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Centrifugal pumps // variable speed

Pump Affinity LawsCalculator

Estimate how flow, head and power change with rotational speed—then compare the theoretical result with the real pump curve, system curve, VFD and process limits.

Reference duty point
m³/h
m
kW
rpm
New speed and energy context
rpm
h
$/kWh

Energy comparison assumes the reference and new duty operate for the same annual hours. It does not model VFD losses, efficiency changes, throttling baseline or a mixed load profile.

Calculated duty at N₂

80.0% of reference speed

FLOW Q₂

80.00 m³/h

HEAD H₂

25.60 m

POWER P₂

9.47 kW

POWER RATIO

51.2%

ENERGY CHANGE

54,168 kWh/y

COST CHANGE

$6,500/y

Q₂ = Q₁ × (N₂ / N₁)
H₂ = H₁ × (N₂ / N₁)²
P₂ = P₁ × (N₂ / N₁)³

Reference-speed scenarios

Flow, head and power do not fall equally

Ideal affinity scaling
SpeedEstimated flowEstimated headEstimated power
110%110.00 m³/h48.40 m24.62 kW
100%100.00 m³/h40.00 m18.50 kW
90%90.00 m³/h32.40 m13.49 kW
80%80.00 m³/h25.60 m9.47 kW
70%70.00 m³/h19.60 m6.35 kW
60%60.00 m³/h14.40 m4.00 kW

When the pump affinity laws apply

The speed relationships are a first estimate for the same centrifugal pump handling the same fluid, with similar hydraulic behavior. They predict how points on the pump curve shift with rotational speed; the actual operating point is where the new pump curve intersects the system curve.

Static head changes the result

A system with substantial static head does not reduce flow in direct proportion to speed at the installed operating point. At low speed the pump may produce too little head to overcome the static component, so the calculated Q₂ is not a guaranteed delivered flow.

Efficiency and NPSH still matter

Pump and motor efficiency change with duty. Check the manufacturer’s speed-specific curves, best-efficiency region, minimum continuous stable flow, NPSH available/required, motor current, bearing/seal limits and VFD minimum/maximum frequency.

Power is not automatically energy saved

The cube relationship shows ideal pump shaft-power scaling. A savings project needs measured baseline power, real operating profile, control method, static head, VFD losses and production requirements. Use the site’s currency and energy tariff for a financial model.