I need the answer quickly Q:For a water/lithium bromide resorption machine shown in the figure (22) below. Aset of operating conditions for the cycle is listed in the table below (table 8.5 in thetext). This set of conditions was generated by imposing mass and energy balanceson the components and the entire cycle. Find:a. Heat transfer rates at the absorber, evaporator, condenser, desorberb. Solution heat exchangers effectiveness.c. System COP.d. Solution and refrigerant pumps work.JUIUn au Igan ypusya wAPO(APa)TO("C)1 ()(% LIBr)(kgrec)(Fraction)0.05000.05000.05000.04590.04590.04590.00410.05000.05000.05000.05410.05410.05410.00411.000056.656.639.739.770.395.61.04510.49098.898.9160.9229.3161.9161.92658.422.510.49010.49010.4901.04556.6Absorber 2Desorber 159.150.484314961.661.661.60.035.40.006SHX210.4901.04510.49010.490SHX 114.935.435.432.822588.9131.470.070.02529.9503.51011121314212223242526272840.2$4.431.810.49010.49032.80.02013.914.9120.01.04532.81.04500490.2116.9Wn1.000025.0104.8117.5104.8112.983.913+28.125.026.920.01.00001.0000Desorber 2Absorber 176.31821428-Figure 22 Resorption Cycleto

a) Heat transfer rates at the absorber, desorber, evaporator and condenser are- QA=m(h24-h23)…

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Engineering

Electrical Engineering

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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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Question

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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

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