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Practical Method for Pump Installation Height Calculation: Including Pipeline Loss and Pump House Requirements

Nov 5,2025
Centrifugal pumps are among the most commonly used pumps for water delivery. The floor elevation in the pump house depends on the installation height of the pump. Accurately calculating the maximum allowable installation height of the pump is of great significance so that the pump station can supply water safely and save on civil engineering costs.


multistage centrifugal pump

To avoid cavitation, the installation height of the centrifugal pump needs to be carefully calculated and verified. A schematic diagram of the pump inlet side assembly is shown below:

 

Pump Installation Location Diagram 

 

   The permissible geometric installation height of a pump depends on various factors, as shown in the following formula:

 

 

 

formula 

 

In the formula:

[Hg] — Permissible geometric installation height of the pump, m; (The calculation result is for design purposes only; the actual installation height must be lower than the permissible installation height)

Pe — Water surface pressure, Pa; (Atmospheric pressure at the water surface, lower at higher altitudes)

Pv — Saturated vapor pressure, Pa; (related to water temperature, the higher the water temperature, the higher the saturated vapor pressure)

ρ—the density of the fluid, kg/m³;

g—acceleration due to gravity, 9.81m/s²;

(NPSH)r—Permissible net positive suction head (NPSH) for the water pump, in meters (m); (Related to pump performance, provided by the pump manufacturer)

hw — Head loss in the suction line, in meters. (Related to the suction line design and determined by the designer)

 


From the above formula, we can see that:

The higher the altitude, the higher the water temperature, the larger the Net Positive Suction Head Required (NPSHr), the greater the head loss in the inlet pipe, and the smaller the allowable geometric installation height.

 

The atmospheric conditions and corresponding water head at different altitudes are shown in the table below:

 

Altitude

(m)

Atmospheric pressure

(kPa)

Head

 (m)

-600

110.85

11.3

0

101.32

10.3

200

99.08

10.1

500

95.16

9.7

1000

90.25

9.2

1500

84.36

8.6

2000

79.46

8.1

3000

70.63

7.2

4000

61.80

6.3

5000

53.95

5.5

 

 

 

 

The table below shows the water head corresponding to the saturated vapor pressure of water at different temperatures:

 

 

 

Water Temperature

( °C )

Saturated Vapor 

Pressure

(kPa)

Head

(m)

10

1.23

0.125

20

2.34

0.238

30

4.24

0.433

40

7.37

0.752

50

12.33

1.272

60

19.92

2.066

70

31.16

3.249

80

47.36

4.97

90

70.10

7.406

100

101.32

10.786

 

 

Example: A certain brand of VISO125X100-315-55/2 water pump has a net positive suction head (NPSHr) of 3.29m. It is intended to operate at an altitude of 500m, where the highest summer water temperature is 40℃. If the head loss in the suction pipe is 1m, the geometric installation height [Hg] of the pump in this location is calculated as follows:

 

Assume the water pressure at the water surface is the local atmospheric pressure, and the atmospheric pressure head at an altitude of 500m is 9.7m from the table;

At a water temperature of 40℃, the saturated vapor head of water is 0.752m;

 

The calculation yields:

[Hg] = 9.7 - 0.752 - 3.29 - 1 = 4.658m

 

Pipeline Loss Calculation Table for Reference




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