Use the design values for the coefficient C, from Table 8.3 unless stated otherwise. Use either of the various forms of the formula or the nomograph in Fig. 8.10 as assigned. 8.63 Water flows at a rate of 1.50 ft/s through 550 ft of 6-in cement-lined ductile iron pipe. Compute the energy loss.
Use the design values for the coefficient C, from Table 8.3 unless stated otherwise. Use either of the various forms of the formula or the nomograph in Fig. 8.10 as assigned. 8.63 Water flows at a rate of 1.50 ft/s through 550 ft of 6-in cement-lined ductile iron pipe. Compute the energy loss.
Chapter2: Loads On Structures
Section: Chapter Questions
Problem 1P
Related questions
Question
Use the design values for the coefficient C, from Table 8.3 unless stated otherwise. Use either of the various forms of the formula or the nomograph in Fig. 8.10 as assigned.
8.63 Water flows at a rate of 1.50 ft/s through 550 ft of 6-in cement-lined ductile iron pipe. Compute the energy loss.
![-
sin frit Idimensionless
Example
Given: 5 in Schedule 40
steel pipe
--00
*-4, 19001 - 20
velocity=110%
SAU TRI MOI QUIERO A
0.275-
bilgil
0.250
0.2233
0.200
0.180
0.100
0.140
0.120
0.100
06.010
0.080
0.03770
0.060
0.0.50
0.045
0.040
0.035
0.010
0.009
4000
EE
0.030 —— 10
0.025 10.9
08
10]
0.030-0.7
AT
3
-15
2
2
14714
-0.6
--03
0.4
0.3
0.25
20
-LIS
NA
www-adid jo jagad
1200
1100--44
1000--40
900 € 30
36
32
28
- 008
100
600
300
500-20
250
200
817
ON
-24
150-60
50
10
-9.0
547-00
- È
33
2.5
20
sin m/m (dimensionless)
an add to MIC
三
-0.13
-0.2
0.3
0.4
0.5
900
15
2.0
40
50
2 3 & SPOR² 2 6 5
LLLLL
Loss of head per 1000 ft (x10³)
Velocity, fus
0.8+0.250
0.9 -0.273
1.0 -0.30
15
20
2.5
3.0
-0.40
FIGURE 8.10 Nomograph for the solution of the Hazen Williams formula for C₁. - 100.
-0.45
-0.30
0.53
0.60
-0.70
0.80
0.90
10
+LI
-1.2
4.5--14
1.3
**
6.0-1.8
1.5
16
6,5-5-20
2.5
CHAP™ LÀ BIG-T Reynolds Number, Laminar Flow, Turbulent Flow, and Energy Losses
GEL ALGOPA
(UWP F
X](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F6419b835-42d6-43f0-a27c-12335eee237b%2Ff1c806b9-d20b-451d-a818-71106433775d%2F01fvpjh_processed.jpeg&w=3840&q=75)
Transcribed Image Text:-
sin frit Idimensionless
Example
Given: 5 in Schedule 40
steel pipe
--00
*-4, 19001 - 20
velocity=110%
SAU TRI MOI QUIERO A
0.275-
bilgil
0.250
0.2233
0.200
0.180
0.100
0.140
0.120
0.100
06.010
0.080
0.03770
0.060
0.0.50
0.045
0.040
0.035
0.010
0.009
4000
EE
0.030 —— 10
0.025 10.9
08
10]
0.030-0.7
AT
3
-15
2
2
14714
-0.6
--03
0.4
0.3
0.25
20
-LIS
NA
www-adid jo jagad
1200
1100--44
1000--40
900 € 30
36
32
28
- 008
100
600
300
500-20
250
200
817
ON
-24
150-60
50
10
-9.0
547-00
- È
33
2.5
20
sin m/m (dimensionless)
an add to MIC
三
-0.13
-0.2
0.3
0.4
0.5
900
15
2.0
40
50
2 3 & SPOR² 2 6 5
LLLLL
Loss of head per 1000 ft (x10³)
Velocity, fus
0.8+0.250
0.9 -0.273
1.0 -0.30
15
20
2.5
3.0
-0.40
FIGURE 8.10 Nomograph for the solution of the Hazen Williams formula for C₁. - 100.
-0.45
-0.30
0.53
0.60
-0.70
0.80
0.90
10
+LI
-1.2
4.5--14
1.3
**
6.0-1.8
1.5
16
6,5-5-20
2.5
CHAP™ LÀ BIG-T Reynolds Number, Laminar Flow, Turbulent Flow, and Energy Losses
GEL ALGOPA
(UWP F
X
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