Environmental Engineering Reference
In-Depth Information
m
21
=˙
˙
m
22
+˙
m
8
(3.3.24)
The energy balance equation for HHX is given below
Q
HHX
m
17a
h
17a
˙
+
=˙
m
21
h
21
(3.3.25)
m
22
h
22
=
Q
HHX
+˙
˙
m
23
h
23
(3.3.26)
The mass and energy balance equations for the condenser are given below
˙
=˙
+˙
m
2
m
6
m
3
(3.3.27)
m
2
h
2
+
Q
con
=˙
˙
m
6
h
6
+˙
m
3
h
3
(3.3.28)
Below mentioned equation is for energy balance of evaporator
Q
eva
m
2a
h
2a
˙
+
=˙
m
1
h
1
(3.3.29)
The following energy balance equation is used to calculate the heat rejected by the
absorber.
m
11
h
11
+
Q
abs
=˙
˙
m
1
h
1
+˙
m
28
h
28
(3.3.30)
The thermal exergy of evaporator and HTG are defined as
1
T
0
T
eva
Ex
th,eva
=
×
Q
eva
−
(3.3.31)
1
T
0
T
HTG
Ex
th,HTG
=
×
Q
HTG
−
(3.3.32)
The energy and exergy COPs are calculated as
Q
eva
Q
HTG
COP
en
=
(3.3.33)
+
W
P
Ex
th,eva
Ex
th,HTG
+
W
P
COP
ex
=
(3.3.34)
Overall energy and exergy efficiencies are defined as
+
Q
eva
m
H
2
×
˙
HHV
η
ov,en
=
×
100
(3.3.35)
I
×
b
×
L
Ex
H
2
×
Ex
th,eva
Ex
so
η
ov,ex
=
×
100
(3.3.36)
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