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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