HAH 4.4.4 An industrial water-distribution system is schematically shown in Figure P4.4.4. The demands on the system are currently at junction D (0.55 m³/s) and E (0.450 m³/s). Water enters the system at junction A from a storage tank (surface elevation of 355.0 m). All pipes are concrete (e = 0.36 mm) with lengths and diameters provided in the table below. In addition, the elevations of the junctions are given in the table. Calculate the flow rate in each pipe (initial estimated flows are provided in Column 2). Solve using the Hardy-Cross method using the the Darcy- Weisbach friction factor. Tabulate each step of the iteration. Also, determine if the pressure at each junction exceeds 185 kPa, a requirement of the water company at the industrial park. Table for HAH 4.4.4 Pipe AB AC BD CE CB ED Flow (m³/sec) Length (m) 0.500 0.500 0.530 0.470 0.030 0.020 300 300 400 400 300 300 Diameter (m) 0.45 0.45 0.40 0.40 0.20 0.20 es elD A 0.00080 0.00080 0.00090 0.00090 0.00180 0.00180 L C A B с 1₂ Figure P4.4.4 Junction HAH 4.4.5 (modified) Repeat HAH 4.4.4 using EPANet and Darcy-Weisbach for head loss. Include screenshots of network and tables as needed Elev. (m) E 355.0 315.5 313.8 313.3 314.1 lD QE

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Chapter2: Loads On Structures
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HAH 4.4.4 An industrial water-distribution system is schematically
shown in Figure P4.4.4. The demands on the system are currently
at junction D (0.55 m³/s) and E (0.450 m³/s). Water enters the
system at junction A from a storage tank (surface elevation of
355.0 m). All pipes are concrete (e = 0.36 mm) with lengths and
diameters provided in the table below. In addition, the elevations
of the junctions are given in the table. Calculate the flow rate in
each pipe (initial estimated flows are provided in Column 2).
Solve using the Hardy-Cross method using the the Darcy-
Weisbach friction factor. Tabulate each step of the iteration.
Also, determine if the pressure at each junction exceeds 185 kPa,
a requirement of the water company at the industrial park.
Table for HAH 4.4.4
Pipe
AB
AC
BD
CB
ED
Flow (m³/sec) Length (m)
0.500
0.500
0.530
0.470
0.030
0.020
300
300
400
400
300
300
Diameter (m)
0.45
0.45
0.40
0.40
0.20
0.20
elD
A
0.00080
0.00080
0.00090
0.00090
0.00180
0.00180
L1
5
B
с
D
E
L₂
Junction
5
Figure P4.4.4
HAH 4.4.5 (modified) Repeat HAH 4.4.4 using EPANet
and Darcy-Weisbach for head loss. Include
screenshots of network and tables as needed
Elev. (m)
lD
355.0
315.5
313.8
313.3
314.1
QE
Transcribed Image Text:HAH 4.4.4 An industrial water-distribution system is schematically shown in Figure P4.4.4. The demands on the system are currently at junction D (0.55 m³/s) and E (0.450 m³/s). Water enters the system at junction A from a storage tank (surface elevation of 355.0 m). All pipes are concrete (e = 0.36 mm) with lengths and diameters provided in the table below. In addition, the elevations of the junctions are given in the table. Calculate the flow rate in each pipe (initial estimated flows are provided in Column 2). Solve using the Hardy-Cross method using the the Darcy- Weisbach friction factor. Tabulate each step of the iteration. Also, determine if the pressure at each junction exceeds 185 kPa, a requirement of the water company at the industrial park. Table for HAH 4.4.4 Pipe AB AC BD CB ED Flow (m³/sec) Length (m) 0.500 0.500 0.530 0.470 0.030 0.020 300 300 400 400 300 300 Diameter (m) 0.45 0.45 0.40 0.40 0.20 0.20 elD A 0.00080 0.00080 0.00090 0.00090 0.00180 0.00180 L1 5 B с D E L₂ Junction 5 Figure P4.4.4 HAH 4.4.5 (modified) Repeat HAH 4.4.4 using EPANet and Darcy-Weisbach for head loss. Include screenshots of network and tables as needed Elev. (m) lD 355.0 315.5 313.8 313.3 314.1 QE
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