Water is to be pumped from one large, open tank to a second large, open tank as shown in Fig. E12.4a. The pipe diameter throughout is 6 in. and the total length of the pipe between the pipe entrance and exit is 200 ft. Minor loss coefficients for the entrance, exit, and the elbow are shown on the figure, and the friction factor for the pipe can be assumed constant and equal to 0.02. A certain centrifugal pump having the performance characteristics shown in Fig. E12.4b is suggested as a good pump for this flow system. With this pump, what would be the flowrate between the tanks? Do you think this pump would be a good choice? (2) K₁= 1.5 10 ft Diameter of pipe = 5 in. Total pipe length = 200 ft Efficiency Head, t Efficiency, % Kt = 0.5 100 80 60 40 20 0 0 1 Head 400 Pump (a) Efficiency 800 1200 1600 2000 2400 Flowrate, gal/min (b) Water K₁ = 1.0 100 de 66.5 Head, ft Efficiency, % 0 Head System curve (Eq. 4). 0 1600 Flowrate, gal/min (c) Operating point 24C
Water is to be pumped from one large, open tank to a second large, open tank as shown in Fig. E12.4a. The pipe diameter throughout is 6 in. and the total length of the pipe between the pipe entrance and exit is 200 ft. Minor loss coefficients for the entrance, exit, and the elbow are shown on the figure, and the friction factor for the pipe can be assumed constant and equal to 0.02. A certain centrifugal pump having the performance characteristics shown in Fig. E12.4b is suggested as a good pump for this flow system. With this pump, what would be the flowrate between the tanks? Do you think this pump would be a good choice? (2) K₁= 1.5 10 ft Diameter of pipe = 5 in. Total pipe length = 200 ft Efficiency Head, t Efficiency, % Kt = 0.5 100 80 60 40 20 0 0 1 Head 400 Pump (a) Efficiency 800 1200 1600 2000 2400 Flowrate, gal/min (b) Water K₁ = 1.0 100 de 66.5 Head, ft Efficiency, % 0 Head System curve (Eq. 4). 0 1600 Flowrate, gal/min (c) Operating point 24C
Chapter2: Loads On Structures
Section: Chapter Questions
Problem 1P
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Question

Transcribed Image Text:Water is to be pumped from one large, open tank to a second large,
open tank as shown in Fig. E12.4a. The pipe diameter throughout is
6 in. and the total length of the pipe between the pipe entrance and
exit is 200 ft. Minor loss coefficients for the entrance, exit, and the
elbow are shown on the figure, and the friction factor for the pipe
can be assumed constant and equal to 0.02. A certain centrifugal
pump having the performance characteristics shown in Fig. E12.4b
is suggested as a good pump for this flow system. With this pump,
what would be the flowrate between the tanks? Do you think this
pump would be a good choice?
(2)
K₁ = 1.5
10 ft
Diameter of pipe = 5 in.
Total pipe length = 200 ft
Efficiency
Head, ft
Efficiency, %
TZ
KL = 0.5
100
80
60
40
20
0
0
Head
400
Pump
(a)
-Efficiency
800
1200 1600 2000 2400
Flowrate, gal/min
Water
K₁ = 1.0
Head, ft
Efficiency, %
100
66.5
Head
System curve (Eq. 4)
0
0
1600
Flowrate, gal/min
Operating
point
2400
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