Service Liquid126.00 Temp.

2100 LPM VicositySp. Gr.Vap. Pres.Density

49.01 kPa 27.31 kPa101.33 kPa(A) 101.33 kPa(A)

4.3 kPa 205.9 kPa146.06 kPa(A) 334.57 kPa(A)

5.57 m 29.03 m5.48 m

Section 1 Section 2 Section 3 Section 4 Section 5Pipe ID (in) 17.25 7.981Pipe ID (m) 0.43815 0.2027174Velocity (m/s) 0.2 1.1Elevation (m) 0.75 0Liq. Head (m) 5.35 0Pipe Length (m) 7.92 49.00Ves. Pres., kPa(G) 0 0

StaticP = 49.01 kPa

PressureP = 101.325 kPa(A)

Friction

Multiplier D (in)Reduced bore 40 mm (112 in.) and smaller

* 65 D 65.00

Reduced bore 50 mm (2 in.) and larger

45 D 45

Standard bore

13 D 13

8

SUCTION

Repea

Ball valve

Rating Head

Head Suction Discharge

PressureFrictionTotalTotal (Differential)NPSH Available

Static

Design Data

Jet Fuel to Refuellerm3/hrDes. Flow

Reduced bore 40 mm (112 in.) and smaller

65 D 65

Straight pattern

340 D 340

Y pattern 160 D 160Angle pattern 145 D 145

Swing type 135 D 135

Ball or piston type 40 mm (112) in. and smaller

340 D 340

Plug valve Regular pattern

45 D 45

Butterfly valve 150 mm (6 in.) and larger

20 D 20

Flow straight-through

20 D 20

Flow through side outlet

65 D 65

90, R = 112 D

20 D 20

45, R = 112 D

16 D 16

90, R = 4 D 14 D 148

90, R = 5 D 16 D 16

180, R = 4 D 25 D 25

180, R = 5 D 28 D 28

Strainer Pump suction Y-type and bucket type

250 D 250

8Entrance/ExitReducerNozzle Suction

nozzle vessel/tank

32 D 32

Control Valve DP = 0 kPaFilter/Separator DP = 0 kPa

Orifice DP = 0 kPa

P friction loss = 0.1* fm * * V2 / (2 * D)

Miscellaneous

*D = nominal size in meters

Fittings

Tee-equal

Elbow

Bend

Valves (fully open)

Gate valve

Globe valve,

Check valve

P friction loss kPa/100m

Section 1 Section 2 Section 3 Section 4 Section 5Pipe ID (in) 17.25 8Pipe ID (m) 0.43815 0.2032Velocity (m/s) 0.2 1.1Pipe Length (m) 7.92 49.00Le (m) (Fittings) 33.5 53.4Reynolds No. 71816 154853 (roughness),mm 0.050 0.050/D 0.00011 0.00025fm 0.0193 0.0176P friction loss (kPa/100m) 0.10 4.13P friction loss (kPa) 0.04 4.23

Calculation of NPSHA

NPSHA = 5.48 m NPSHR = xxx m

(From Performance Curve)

Check if NPSHA > NPSHR Acceptable??

Calculation of Hydraulic Power

hyd kW = 7.59 kW

Calculation of Actual Power

Pump Efficiency = 70 % (From Curve at Rated Flow) bkW = 10.8 bkW

Motor SizingAt run-out (end of Head curve for impeller D' mm diameter)

Pump Efficiency = % (From Head Curve at run-out)

Maximum flow = m3/hr Total Head = m

#DIV/0! kW

Choose a Motor o YYY kW for full curve protection (POWER CURVE

35 oC 120 m3/hr in ITB1.16 cp0.82

0.7 kPa819.18 kg/m3

-21.69 kPa0.00 kPa

201.66 kPa188.51 kPa

23.5 m27.0 m

Section 6 Section 7 Section 8 Section 1 Section 2Pipe ID (in) 17.25 6.025Pipe ID (m) 0.43815 0.153035Velocity (m/s) 0.2 1.9Elevation (m) 0.5 1.6Liq. Head (m) 0 1.8Pipe Length (m) 3.2 3Ves. Pres., kPa(G) 0 0

Static (kPa)P = 27.31 kPa

Pressure, kPa(A)P = 101.325 kPa(A)

Friction

D (m) Pieces Le (Total), m

0 0

Reduced bore 40 mm (112 in.) and smaller

0 0

Reduced bore 50 mm (2 in.) and larger

0.2032 1 2.6416

Standard bore

at Calculating Each Pipe Section

Ball valve

Differential

Hydarulics and Centrifugal Pump Sizing

Jet Fuel-A1

0 0

Reduced bore 40 mm (112 in.) and smaller

0 0Straight pattern

0 0 Y pattern

0 0Angle pattern

0 0Swing type

0 0

Ball or piston type 40 mm (112) in. and smaller

0 0Plug valve Regular

pattern

0 0

Butterfly valve 150 mm (6 in.) and larger

0 0

Flow straight-through

0 0Flow through side outlet

0 090, R = 112 D

0 045, R = 112 D

0.2032 3 8.534490, R = 4 D

0 090, R = 5 D

0 0180, R = 4 D

0 0180, R = 5 D

0.2032 1 50.8

Strainer Pump suction Y-type and bucket type

Entrance/Exit KReducer

0 0

Nozzle Suction nozzle vessel/tank

Total 61.976

Control Valve DP = 40 kPaFilter/Separator DP = 105 kPa

Orifice DP = 10 kPa

P friction loss = 0.1* fm * * V2 / (2 * D)

Miscellaneous

*D = nominal size in meters

Fittings

Tee-equal

Elbow

Bend

Valves (fully open)

Gate valve

Globe valve,

Check valve

P friction loss kPa/100m

Section 6 Section 7 Total Section 1 Section 2Pipe ID (in) 6.025 17.25Pipe ID (m) 0.153035 0.43815Velocity (m/s) 1.9 0.2Pipe Length (m) 168.8 3.2Le (m) (Fittings) 94.1 0.0Reynolds No. 205614 71816 (roughness),mm 0.050 0.050/D 0.00033 0.00011fm 0.02 0.0195P friction loss (kPa/100m) 19.38 0.098

4.27 P friction loss (kPa) 50.93 0.003

E * ACTUAL Rel. Density of the Power Curve)

Section 3 Section 4 Section 5 Section 6 Section 7 Section 86.025

0.1530351.90.5

0165.8

0

Multiplier D (in) D (m) Pieces Le (Total), m* 65 D 65.00

0 045 D 45

6 0.1524 1 6.85813 D 13

6 0.1524 3 5.9436

DISCHARGE

Repeat Calculating Each Pipe Section

65 D 65

0 0340 D 340

0 0160 D 160 0 0145 D 145

0 0135 D 135

6 0.1524 1 20.574340 D 340

0 045 D 45

0 020 D 20

0 020 D 20

0 0 065 D 65

0 0 020 D 20

6 0.1524 6 18.28816 D 16

0 014 D 14

6 0.1524 2 4.267216 D 16

0 025 D 25

0 028 D 28

0 0250 D 250

6 0.1524 1 38.10.05 0.009228 2 0.018455018

32 D 32

0 0Total 94.04925502

Section 3 Section 4 Section 5 Section 6 Section 7 Total

205.93

Sizing Calculation