Ans) Given,
Discharge = 3 cfs
Elevation difference (Z) = 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 / g) - z - HL - (Pv/g)
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 / g) - NPSH - HL - (Pv/g)
We know,
Q = A x V
=> V = Q/A = 3 / (/4) (0.5)2 = 15.28 ft/s
Reynold number , Re = VD/
where, = 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 = K 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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