How to select a centrifugal pump

Calculation example for the selection of a centrifugal pump

Case A Istallation data

- Q (Flow) = 42 m

3

/h

- Hga (geometric head inlet) = 3,5 m

- Hgp (geometric head outlet) = 39 m

- 5 m DN 100 mm diameter suction pipe complete with 1 elbow

and 1 foot valve

- 70 m DN 80 mm diameter delivery pipe with 1 non-return valve, 1

gate valve and 3 sweep elbows

Hg = Hgp + Hga = 39 + 3,5 = 42,5 m Geometric head of the installa-

tion

A) Operation with suction lift

Hg

Δpc = total head loss

Suction side:

5 m Ø100 piping

1 Elbows

1 Foot valve

Delivery side:

70 m Ø 80 pipe

1 Non-return valve

1 Gate valve

3 Elbows

Total

pc = 0,12 m

pc = 0,045 m

pc = 0,46 m

pc = 5,25 m

pc = 0,5 m

pc = 0,05 m

pc = 0,09 m

Δpc = 6,5 m.

Ø 80 Pipe

70 m Length

4.93.180.1

Ø 100 Pipe

5 m Length

Foot valve

B) Operation under positive suction head

Hg

Hgp

Hga

Considering that the calculation has been made for new pipes, an

increase of 15/20% is to be applied for ageing etc. Therefore the

total head loss Δp amounts to about 8 m.

Therefore, the total manometric head which the pump must achieve is:

Hmt = Hg + Δp = Hgp + Hga + Δpc = 39 + 3,5 + 8 = 50,5 m total.

The pump type NM 50/20AE can be chosen (see pump diagram)

Case B Istallation data

- Q (Flow) = 42 m

3

/h

- Hga (geometric head inlet) = 3,5 m

- Hgp (geometric head outlet) = 39 m

- 5 m DN 100 mm diameter suction pipe complete with 1 gate valve

and 1 foot valve

- 70 m DN 80 mm diameter delivery pipe with 1 non-return valve, 1

gate valve and 3 sweep elbows

Hg = Hgp - Hga = 39 - 3,5 = 35,5 m Geometric head of the installation

Δpc = total head loss

Suction side:

5 m Ø 100 piping

1 Non-return valve

1 Gate valve

Delivery side:

70 m Ø 80 pipe

1 Non-return valve

1 Gate valve

3 Elbows

Total

pc = 0,12 m

pc = 0,5 m

pc = 0,05 m

pc = 5,25 m

pc = 0,5 m

pc = 0,05 m

pc = 0,09 m

Δpc = 6,5 m

Considering that the calculation has been made for new pipes, an

increase of 15/20% is to be applied for ageing etc. Therefore the

total head loss Δpc amount to about 8 m.

Therefore, the total manometric head which the pump must achieve is:

Hmt = Hg + Δp = Hgp - Hga + Δpc = 39 - 3,5 + 8 = 43,5 m total.

Hgp

Hga

Ø 80 Pipe

70 m Length

4.93.100

Ø 100 Pipe

5 m Length

492