The head or pressure of a centrifugal pump can be expressed like
dp 1 / dp 2 = (n 1 / n 2 ) 2 (d 1 / d 2 ) 2 (2)
where
dp = head or pressure (m, ft, Pa, psi, ..)
The power consumption of a centrifugal pump can be expressed as
P 1 / P 2 = (n 1 / n 2 ) 3 (d 1 / d 2 ) 3 (3)
where
P = power (W, bhp, ..)
If the wheel diameter is constant - change in pump wheel velocity can simplify the affinity laws to
q 1 / q 2 = (n 1 / n 2 ) (1a)
dp 1 / dp 2 = (n 1 / n 2 ) 2 (2a)
P 1 / P 2 = (n 1 / n 2 ) 3 (3a)
Note! If the speed of a pump is increased with 10%
If we want to increase the volume flow capacity of an existing system with 10% we have to increase the power supply with 33% .
Replace the default values with the actual values. The calculator is generic and can be used with all common units as long as the use is consistent.
If wheel velocity is constant a change in impeller diameter simplifies the affinity laws to
q 1 / q 2 = d 1 / d 2 (1b)
dp 1 / dp 2 = (d 1 / d 2 ) 2 (2b)
P 1 / P 2 = (d 1 / d 2 ) 3 (3b)
Replace the default values with the actual values. The calculator is generic and can be used with all common units as long as the use of units is consistent.
The pump speed is changed when the impeller size is constant. The initial flow is 100 gpm , the initial head is 100 ft , the initial power is 5 bhp , the initial speed is 1750 rpm and the final speed 3500 rpm .
The final flow capacity can be calculated with (1a):
q 2 = q 1 n 2 / n 1
= (100 gpm) (3500 rpm) / (1750 rpm)
= 200 gpm
The final head can be calculated with (2a):
dp 2 = dp 1 (n 2 / n 1 ) 2
= (100 ft) ((3500 rpm) / (1750 rpm)) 2
= 400 ft
The final power consumption can be calculated with (3a):
P 2 = P 1 (n 2 / n 1 ) 3
= (5 bhp) ((3500 rpm) / (1750 rpm)) 3
= 40 bhp
The diameter of the pump impeller is reduced when the pump speed is constant. The diameter is changed from 8 to 6 inches .
The final flow capacity can be calculated with (1b) :
q 2 = q 1 (d 2 / d 1 )
= (100 gpm) ((¨6 in) / (8 in))
= 75 gpm
The final head can be calculated with (2b) :
dp 2 = dp 1 (d 2 / d 1 ) 2
= (100 ft) ((6 in) / (8 in)) 2
= 56.3 ft
The final power consumption can be calculated with (3b) :
P 2 = P 1 (d 2 / d 1 ) 3
= (5 bhp) ((6 in) / (8 in)) 3
= 2.1 bhp
The volume capacity can be expressed like
q 1 / q 2 = (n 1 / n 2 )(d 1 / d 2 ) 3 (4)
where
q = volume flow capacity (m 3 /s, gpm, cfm, ..)
n = wheel velocity - revolution per minute - (rpm)
d = wheel diameter
The head or pressure of a centrifugal pump can be expressed like
dp 1 / dp 2 = (n 1 / n 2 ) 2 (d 1 / d 2 ) 2 (5)
where
dp = head or pressure (m, ft, Pa, psi, ..)
The power consumption of a centrifugal pump can be expressed as
P 1 / P 2 = (n 1 / n 2 ) 3 (d 1 / d 2 ) 5 (6)
where
P = power (W, bhp, ..)
Note that the affinity laws for fans are not identical with pumps.
The study of fluids - liquids and gases. Involving velocity, pressure, density and temperature as functions of space and time.
Piping systems and pumps - centrifugal pumps, displacement pumps - cavitation, viscosity, head and pressure, power consumption and more.
An introduction to Centrifugal Pumps.
Modulating pumps to adapt capacities to variable process demands.
Minimum continuous flow to prevent flashing in centrifugal pumps.
Centrifugal pumps and maximum shut-off head.
The affinity laws can be used to calculate resulting volume capacity, head or power consumption when speed or wheel diameters are changed.
Horsepower required to pump water.
An introduction to pumps and the Net Positive Suction Head (NPSH).
Characterizing of impeller types in pumps in a unique and coherent manner.
Suction Specific Speed can be used to determine stable and reliable operations for pumps with max efficiency without cavitation.
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