Pump Specific Speed (Ns)

Ns=NQH0.75N_s = \frac{N \sqrt{Q}}{H^{0.75}}

Worked example: 1750 rpm, 500 gpm, 100 ft → Ns = 1237.4 — press Try an example to run it live, then adjust anything.

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Pump Specific Speed (Ns) explained

NQHNs

Specific speed answers a question the duty point alone cannot: what shape of impeller does this job want? Combine speed, flow and head into one index at the best efficiency point and the geometry falls out. Below about Ns = 1500 you want a radial impeller — narrow, large-diameter, high head, low flow. Between roughly 2000 and 5000 the impeller becomes mixed-flow, and above about 9000 it is an axial propeller, all flow and almost no head. A 1750 rpm pump making 100 ft at 500 gpm has Ns=1750×500/1000.75≈1237\mathrm{Ns} = 1750 \times \sqrt{500} / 100^{0.75} \approx 1237: a classic end-suction radial machine.

Ns as written is not dimensionless despite being quoted as a bare number — the value depends entirely on the units, and the US convention (rpm, gpm, ft) that this page evaluates gives numbers roughly 51.6 times the metric (rpm, m³/s, m) convention. Always state which you mean. There is also a sibling worth knowing: suction specific speed, S=NQ/NPSHr0.75S = N\sqrt{Q}/\mathrm{NPSHr}^{0.75}, where values above about 11 000 flag a pump that will be unstable and cavitation-prone away from its best efficiency point, a lesson the refining industry learned expensively in the 1970s.

Pump Specific Speed (Ns) formula

Ns=NQH0.75N_s = \frac{N \sqrt{Q}}{H^{0.75}}
Where
  • NsN_s= Specific speed (US convention) (rpm·√gpm/ft^0.75)
  • NN= Pump speed (Hz)
  • QQ= Flow at BEP (L/min)
  • HH= Head at BEP (m)

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