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Introductory Circuit Analysis (13th Edition)
13th Edition
ISBN:9780133923605
Author:Robert L. Boylestad
Publisher:Robert L. Boylestad
Chapter1: Introduction
Section: Chapter Questions
Problem 1P: Visit your local library (at school or home) and describe the extent to which it provides literature...
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Q:
For a water/lithium bromide resorption machine shown in the figure (22) below. A
set of operating conditions for the cycle is listed in the table below (table 8.5 in the
text). This set of conditions was generated by imposing mass and energy balances
on the components and the entire cycle. Find:
a. Heat transfer rates at the absorber, evaporator, condenser, desorber
b. Solution heat exchangers effectiveness.
c. System COP.
d. Solution and refrigerant pumps work.
JUIUn au Igan ypusya wA
PO
(APa)
TO
("C)
1 ()
(% LIBr)
(kgrec)
(Fraction)
0.0500
0.0500
0.0500
0.0459
0.0459
0.0459
0.0041
0.0500
0.0500
0.0500
0.0541
0.0541
0.0541
0.0041
1.0000
56.6
56.6
39.7
39.7
70.3
95.6
1.045
10.490
98.8
98.9
160.9
229.3
161.9
161.9
2658.4
22.5
10.490
10.490
10.490
1.045
56.6
Absorber 2
Desorber 1
59.1
50.4
843
149
61.6
61.6
61.6
0.0
35.4
0.006
SHX2
10.490
1.045
10.490
10.490
SHX 1
14.9
35.4
35.4
32.8
225
88.9
131.4
70.0
70.0
2529.9
503.5
10
11
12
13
14
21
22
23
24
25
26
27
28
40.2
$4.4
31.8
10.490
10.490
32.8
0.020
13.9
14.9
120.0
1.045
32.8
1.045
00
490.2
116.9
Wn
1.0000
25.0
104.8
117.5
104.8
112.9
83.9
13+
28.1
25.0
26.9
20.0
1.0000
1.0000
Desorber 2
Absorber 1
76.3
182
14
28-
Figure 22 Resorption Cycle
to
Transcribed Image Text:Q: For a water/lithium bromide resorption machine shown in the figure (22) below. A set of operating conditions for the cycle is listed in the table below (table 8.5 in the text). This set of conditions was generated by imposing mass and energy balances on the components and the entire cycle. Find: a. Heat transfer rates at the absorber, evaporator, condenser, desorber b. Solution heat exchangers effectiveness. c. System COP. d. Solution and refrigerant pumps work. JUIUn au Igan ypusya wA PO (APa) TO ("C) 1 () (% LIBr) (kgrec) (Fraction) 0.0500 0.0500 0.0500 0.0459 0.0459 0.0459 0.0041 0.0500 0.0500 0.0500 0.0541 0.0541 0.0541 0.0041 1.0000 56.6 56.6 39.7 39.7 70.3 95.6 1.045 10.490 98.8 98.9 160.9 229.3 161.9 161.9 2658.4 22.5 10.490 10.490 10.490 1.045 56.6 Absorber 2 Desorber 1 59.1 50.4 843 149 61.6 61.6 61.6 0.0 35.4 0.006 SHX2 10.490 1.045 10.490 10.490 SHX 1 14.9 35.4 35.4 32.8 225 88.9 131.4 70.0 70.0 2529.9 503.5 10 11 12 13 14 21 22 23 24 25 26 27 28 40.2 $4.4 31.8 10.490 10.490 32.8 0.020 13.9 14.9 120.0 1.045 32.8 1.045 00 490.2 116.9 Wn 1.0000 25.0 104.8 117.5 104.8 112.9 83.9 13+ 28.1 25.0 26.9 20.0 1.0000 1.0000 Desorber 2 Absorber 1 76.3 182 14 28- Figure 22 Resorption Cycle to
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