Suction Specific Speed can be used to determine stable and reliable operations for pumps with max efficiency without cavitation.
Suction Specific Speed - Nss - can be useful when evaluating the operating conditions on the suction side of pumps. Suction Specific Speed is used to determine what pump geometry - radial, mixed flow or axial - to select for a stable and reliable operation with max efficiency without cavitation. Nss can also be used to estimate safe operating ranges.
Suction Specific Speed is a dimensionless value and can be calculated as
Nss = ω q1/2 / NPSHr3/4 (1)
Nss = Suction Specific Speed
ω = pump shaft rotational speed (rpm)
q = flow rate capacity (m3/h, l/s, m3/min, US gpm, British gpm) - for the pump at Best Efficiency Point (BEP)
Nss have the same value for geometrically similar pumps. As a rule of thumb the Specific Suction Speed should be below 9000 (calculated with US gpm) to avoid cavitation and unstable and unreliable operations. Empirical studies indicates that safe operating ranges from Best Efficiency Points (BEP) are more narrow at higher Suction Specific Speeds.
Specific Suction Speed - Nss - Pump Calculator
This calculator can be used to calculate the Suction Specific Speed for a pump.
Note! When comparing pumps and their documentation - be aware of the units used.
Convert between Imperial units (gpm) and Metric units (m3/h, l/s)
- Nss (US gpm) = 1.63 Nss (metric l/s) = 0.86 Nss (metric m3/h)
- Nss (Metric l/s) = 0.614 Nss (US gpm)
- Nss (Metric l/s) = 0.67 Nss (British gpm)
Example - Actual NPSHa vs Required NPSHr
For a pump with flow 1000 gpm, head 500 ft, speed 3000 rpm and a maximum acceptable Suction Specific Speed 9000 - the Required Net Positive Suction Head can be calculated by modifying (1) as
NPSHr = (ω q1/2 / Nss)4/3
= ((3000 rpm) (1000 gpm)1/2 / (9000))4/3
= 23 ft
The calculated Required Net Positive Suction Head - NPSHr - is the minimum head required for proper operation. It is common to add a safety margin when calculating the Actual Net Positive Suction Head - NPSHa - for the installation.
NPSHa = NPSHr Sr (2)
Sr = safety ratio
For the example above we assume the safety ratio Sr to be 1.5 (50%). Actual NPSHa with the safety margin can then be calculated to
NPSHa = (23 ft) (1.5)
= 34.5 ft
Note that if the head at the suction side of the pump is lower than the required NPSHa - the head can be increased by
- increasing the dimensions on the suction pipes
- shorten the suction pipes
- remove or reduce the number of components like valves or filters in the suction pipes
- increase the static pressure in the system
- lower the pump (increasing the static pressure in the pump)
Example - Suction Specific Speed
For a pump the actual Net Positive Suction Head - NPSHa - available in the process line is determined to 20 ft. For a pump with rotational speed 1750 rpm and flow rate 500 US gpm - the operating Suction Specific Speed with this NPSHa can be estimated to
Nss = (1750 rpm) (500 gpm)1/2 / (20 ft)3/4
- well below the limit 9000 to avoid cavitation
We can use the same safety margin as in the example above and calculate NPSHr by modifying (2) to
NPSHr = NPSHa / Sr
= (20 ft) / (1.5)
= 13.3 ft
Double Suction Type Pumps
For a double suction pump the flow at the inlet is divided by two. Using a double suction pump is one way of meeting system NPSH and obtaining a higher head.