*For questions a) and b), you must answer directly on the graph on the next page when required to do so (figure 2.2)* You must pump 5°C water from a large open-air reservoir to another at a rhythm of 1 1/s. The pipe linking both reservoirs is one inch in diameter, has a Hazen-Williams coefficient of 140 and measures 1 km (975 m of which are found after the pump displayed on figure 2.1). Singular head loss can be neglected. Based on figures 2.1 and 2.2, you must: a) Select the most adequate pump to complete your project: b) Identify the point of operation (minimum 3 points must be calculated on the pipe characteristic curve); c) Determine if cavitation could be an issue. N.B. presume atmospheric pressure to be 101.3 kPa.

Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
ChapterMA: Math Assessment
Section: Chapter Questions
Problem 1.1MA
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*For questions a) and b), you must answer directly on the graph on the next page when required
to do so (figure 2.2)*
You must pump 5°C water from a large open-air reservoir to another at a rhythm of 1 1/s. The pipe
linking both reservoirs is one inch in diameter, has a Hazen-Williams coefficient of 140 and measures 1
km (975 m of which are found after the pump displayed on figure 2.1).
Singular head loss can be neglected.
Based on figures 2.1 and 2.2, you must:
a) Select the most adequate pump to complete your project:
b) Identify the point of operation (minimum 3 points must be calculated on the pipe characteristic
curve);
c) Determine if cavitation could be an issue.
N.B. presume atmospheric pressure to be 101.3 kPa.
6 m
Figure 2.1 Pump configuration
P
2 m
15 m
Transcribed Image Text:*For questions a) and b), you must answer directly on the graph on the next page when required to do so (figure 2.2)* You must pump 5°C water from a large open-air reservoir to another at a rhythm of 1 1/s. The pipe linking both reservoirs is one inch in diameter, has a Hazen-Williams coefficient of 140 and measures 1 km (975 m of which are found after the pump displayed on figure 2.1). Singular head loss can be neglected. Based on figures 2.1 and 2.2, you must: a) Select the most adequate pump to complete your project: b) Identify the point of operation (minimum 3 points must be calculated on the pipe characteristic curve); c) Determine if cavitation could be an issue. N.B. presume atmospheric pressure to be 101.3 kPa. 6 m Figure 2.1 Pump configuration P 2 m 15 m
0
350+
H
m
300
250-
200
150
100
50
0
70
60
de
20+
D
4GS
I
Imp gpm
US 9pm
1
I
5
I
5
20
L
I I
T
I
I
I L
10
L
40
2900 rpm
10
1
I L I
15
4G$40
4GS30
4GS22
4GS15
4GS11
4GS07
4GS05
4GS03
70%
60
I
I
ISO 9906-Annex A
L
20
Figure 2.2 Pump catalog excerpt (answer directly on the graph)
T
I
20
I
25
80 Q 1/min
H
Ft
- 1000
-800
-600
400
200
100
5 Q m²/h 6
.0
017369_A_CH
Transcribed Image Text:0 350+ H m 300 250- 200 150 100 50 0 70 60 de 20+ D 4GS I Imp gpm US 9pm 1 I 5 I 5 20 L I I T I I I L 10 L 40 2900 rpm 10 1 I L I 15 4G$40 4GS30 4GS22 4GS15 4GS11 4GS07 4GS05 4GS03 70% 60 I I ISO 9906-Annex A L 20 Figure 2.2 Pump catalog excerpt (answer directly on the graph) T I 20 I 25 80 Q 1/min H Ft - 1000 -800 -600 400 200 100 5 Q m²/h 6 .0 017369_A_CH
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