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NPSH and Pump Head Calculation for Water Supply Systems

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Dedi Sumaha Wijaya

Academic year: 2025

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Discharge

3000 HMax. Liquid Level, mm

1000 64 meter

OPERATING CONDITIONS Pump Name Tag. No Fluid Name Temp. Nor. oC SG Nor.

Acceleration of gravity (m/s2) Vapor Press. Nor. kg/cm2 Viscosity Nor. cP

Normal Capacity m3/h 133 l/s

Number of Pumps in Operation

Total Flow 266,000 l/s

Cap. Overdesign %

Rated Capacity m3/h DISCHARGE CONDITIONS

Size

SUCTION CONDITIONS 12"

Pipe Size 24"

Pipe 1 24"

Pipe 2

Min. Drum Press. kg/cm2g Pressure Loss

Min. Static Head kg/cm2g 0,299 Max. a. Line & Fittings kg/cm2

Pressure Loss b. Orifice/FE kg/cm2

a. Line & Fittings kg/cm2 (Table 1) c. Elevation kg/cm2

b. Strainer kg/cm2 d. Equipment kg/cm2

c. Other Loss kg/cm2 e. Allowance 10% kg/cm2

Suc. Pressure kg/cm2g 0,179 Max. f. Control Valve kg/cm2

Max. Desti. Press. kg/cm2g

DIFFERENTIAL PRESSURE Disch. Pressure kg/cm2g

Disch. Pressure kg/cm2g

Suc. Pressure kg/cm2g BRAKE HORSEPOWER

Special Margin kg/cm2 Pump Eff. %

Diff. Pressure kg/cm2 BHP = Cap. Design x SG x Head/367/ Eff.

Head m

Proposed Pump Head m BHP kW

NET POSITIVE SUCTION HEAD Suc. Pressure kg/cm2g Vap. Press. - 1.033 kg/cm2g Net kg/cm2 NPSHA m

NPSHR Pump m Min NPSHR ( 1.5 meter < NPSHA )

Note :

64000 Min. Liquid Level, mm

UPSTREAM LHOKSEUMAWE DRINKING WATER SUPPLY SYSTEM

NPSH A & PUMP HEAD REQUIRED CALCULATION

Issued 20-Jun-24 CALCULATION SHEET Rev. 0 Page : 1 of 2

m3/h 957,60

Intake PUMP P-101, P-102, P-103

Water 30 998,2 Suction

Max. Liquid Level, mm

0,0 957,60

Pipe ID (mm) Velocity (m/s)

Pipe 3 304,9 1,82

9,806 0,042 0,860 478,80 2

ID (mm) Velocity (m/s) Pipe 4 554,0 1,10

250,00 2,71 Pipe 5 554,0 1,10

0,100 (Table 3) 0,588

0,020

0,000 6,388

250,00 2,71

0,000

0,200

CALCULATION 7,896

7,896

0,120 0,000

0,000 0,700

-0,020 0,000

7,916

79,182 <====

80 127,78

-0,020 CALCULATION

0,000 81,53

-0,991 0,971 CALCULATION

-0,020

9,711 8,211

AERASI DN 630"

FT

EL +4.00 DN 300"

DN 300"

H

EL_+60

DN 630"

EL_+68

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Table 3. Pressure Drop Calculation for Discharge

Pipe Pipe

Nominal Size (in) Nominal Size (in)

SG SG

Viscocity (cP) Viscocity (cP)

Flow (m3/h) Flow (m3/h)

Flow (kg/h) Flow (kg/h)

Line Length (m) Line Length (m)

Roughness Roughness

ID (mm) ID (mm)

Velocity Velocity

Re Re

f f

Pressure Drop/100 m (kg/cm2) Pressure Drop/ 100 m (kg/cm2)

Act. Length + margin 10% (m) Act. Length + margin 5% (m)

Equiv. Length + margin 0% (m) Equiv. Length + margin (m)

Line Loss K (ft) method (kg/cm2) Line Loss K (ft) method (kg/cm2)

Total line loss (kg/cm2) Total line loss (kg/cm2)

Table 4. Equivalent Length Calculation for Discharge

Fittings Qty Qty Eq. Length, m Fittings Qty Qty Qty

Gate Valve 0 0 0

0 0 0,00 Butterfly Valve 1 0 2

Butterfly Valve 0 0 0,00 Tee (Flow Straight) 1 0 2

Tee (Flow Straight) 0 0 0,00 Elbow 45 2 20 20

Tee (Flow Turns) 0 0 0,00 Elbow 90 2 10 10

Elbow 90 0 0 0,00 Sudden Enlargement 1 1 0 0

Elbow 45 0 0 0,00 Sudden Enlargement 2 0 0 0

Reducer 32 x 18 0 0 0,00 Sudden Enlargement 3 0 0 0

Reducer 30 x 24 0 0 0,00 Check Valve 1 0 0

Reducer 1 1 0 0

Reducer 2 0 0 0

Reducer 3 0 0 0

Total

Table 5. Representative Resistance Coefficients (K) for Valves and Fittings

K = L/D

Table 6. Pressure Drop Across Control Valve

Gate Valve

8

Control Valve

Check Valve - Swing Type

100

Nominal Size (in)

Globe Valve

340

SG

Check Valve - Ball Type

150

Flow Coefficient of Valve (Cv)

Tilting Disc Check Valve

40

Flow (m3/h)

Foot Valve - Hing Disk Type

75

Number Of Valve (Pcs)

Ball Valve

18

Pressure Drop of Control Valve (kg/cm2)

Butterfly Valve

45

Total Pressure Drop (kg/cm2)

Standard Elbow 45

16

Standard Elbow 90

30

Standard Tee (Turn) with flow throught branch

60

Standard Tee (Straight) with flow throught Run

20

Note :

NPSH A & PUMP HEAD REQUIRED CALCULATION

Issued 20-Jun-24 CALCULATION SHEET Rev. 0 Page : 2 of 2

UPSTREAM LHOKSEUMAWE DRINKING WATER SUPPLY SYSTEM

Pipe 5

0 0 12" 24" 24"

SUCTION DISCHARGE

Table 1. Pressure Drop Calculation for Suction

Pipe 1 Pipe 2 Pipe 3 Pipe 4

0,860 0,860 0,860 0,860 0,860

998,200 998,200 998,2 998,2 998,2

477938 477938 477938 955876 955876

478,80 478,80 478,80 957,60 957,60

0,0015 0,0015 0,0015 0,0015 0,0015

0,00 0,00 10,00 20,00 3500,00

2,71 2,71 1,82 1,10 1,10

250,00 250,00 304,9 554,0 554,0

0,0106 0,0122 0,0126 0,0123 0,0123

786214 786214 644649 709580 709580

0,00 0,00 10,50 21,00 3675,00

1,5884 0,1820 0,0695 0,0138 0,0138

0,0000 0,0000 0,00 0,04 0,55

0,00 0,00 152,28 246,20 318,22

Pipe 5

Size 0,0 0,0 Size 12" 24" 24"

0,0000 0,0000 0,5883

Table 2. Equivalent Length Calculation for Suction

Pipe Pipe 1 Pipe 2 Pipe Pipe 3 Pipe 4

Eq. Length, m Eq. Length, m Eq. Length, m Eq. Length, m

0,00 0,00 0,00

Gate Valve 0,00 13,72 0,00 49,86

0,00 6,10 0,00 22,16

0,00 36,60 0,00 0,00

0,00 0,00 0,00 0,00

0,00 8,00 80,00 80,00

0,00 18,29 166,20 166,20

Total 0,00 0,00 39,08 0,00 0,00

0,00 0,00 0,00 0,00

0,00 30,49 0,00 0,00

318,22

Valves and Fittings

C.Valve 1

0,00 0,00 0,00

0,00 0,00 0,00

0,000 24"

0,86 3400 340,00

0 0,012

152,28 246,20

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