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Problem 4 The pumping system shown in the figure below to deliver 3 cfs of 60°F water. The total elevation difference between
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Answer #1

Ans) Given,

Discharge = 3 cfs

Elevation difference (\DeltaZ) = 84 ft

Diameter of pipe at inlet and outlet , D1 = D2 = 6 in or 0.5 ft

Length of pipe 1 = 300 ft

Length of pipe 2 = 860 ft

Suction inlet height = 20 ft

NPSH = 7 ft

We know,

NPSH = (Patm / \rhog) - z - HL - (Pv/\rhog)

where, z = maximum height that pump can be placed without cavitation

Pv = Vapor pressure of water at 60 F = 0.256 psia

HL = head loss due to friction , valves and elbows

=> zmax = (Patm / \rhog) - NPSH - HL - (Pv/\rhog)

We know,  

Q = A x V

=> V = Q/A = 3 / (\pi/4) (0.5)2 = 15.28 ft/s

Reynold number , Re = \rhoVD/\mu

where, \mu = dynamic viscosity of water at 60 F = 2.3 x 10-5

=> Re = 1.94 x 15.28 x 0.5 / 2.3 x 10-5

=> Re = 6.4 x 105

Roughness of cast iron pipe,e = 0.01 in or 0.00085 ft

Relative roughness = e/D = 0.00085/0.5 = 0.0017

According to Moody diagram, for Re = 6.4 x 105 and e/D = 0.0017. friction factor (f) = 0.023

=> Head loss due to friction = f L V2 / 2gD = 0.023(300)(15.28)2 / ( 2 x 32.2 x 0.5)

=> Head loss due to friction = 50.02 ft

Minor loss = \sumK V2 / 2g = (0.5 + 0.23 + 0.67) (15.28)2 / ( 2 x 32.2)

Minor loss = 1.4 x 233.47 / 64.4 = 5.07 ft

=> HL = 50.02 + 5.07 = 55.09 ft

Putting values in above equation,

zmax = (14.7 x 144 / 62.2) - 7 - 55.09 - (0.256 x 144/ 62.2)

=> zmax = 34.08 - 7 - 55.09 - 0.592

=> zmax = 28.6 ft > 20 ft

Since, maximum allowable height of pump is larger than 20 ft, pump will not suffer cavitation  

  

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