GAS POWER CYCLES 647
dharm
\M-therm\Th13-3.pm5
For the constant volume process 2-3,
p
T
p
T
2
2
3
3
=
∴ T 3 = T 2 ×
p
p
3
2
= 874.1 ×
68
21 67.
= 2742.9 K. (Ans.)
Heat added at constant volume
= cv (T 3 – T 2 ) = 0.71 (2742.9 – 874.1) = 1326.8 kJ/kg
∴ Heat added at constant pressure
= Total heat added – heat added at constant volume
= 1750 – 1326.8 = 423.2 kJ/kg
∴ cp(T 4 – T 3 ) = 423.2
or 1.0(T 4 – 2742.9) = 423.2
∴ T 4 = 3166 K. (Ans.)
For constant pressure process 3-4,
ρ =
V
V
T
T
4
3
4
3
= =^3166
2742.9
= 1.15
For adiabatic (or isentropic) process 4-5,
V
V
V
V
V
V
V
V
V
V
5 r
4
5
2
2
4
1
2
3
4
=×=×=
ρ Q ρ=
F
HG
I
KJ
V
V
4
3
Also p 4 V 4 γ = p 5 V 5 γ
∴ p 5 = p 4 × V
V
4
5
F
HG
I
KJ
γ
= 68 ×
ρ γ
r
F
HG
I
KJ = 68 ×
115
9
.^14.
F
HG
I
KJ = 3.81 bar. (Ans.)
Again, T
T
5
4
=
V
Vr
4
5
(^11141)
115
9
F
HG
I
KJ
=GFH IKJ =FHG IKJ
γ− γ−−
ρ..
= 0.439
∴ T 5 = T 4 × 0.439 = 3166 × 0.439 = 1389.8 K. (Ans.)
(ii)Air standard efficiency :
Heat rejected during constant volume process 5-1,
Qr = cv(T 5 – T 1 ) = 0.71(1389.8 – 363) = 729 kJ/kg
∴ ηair standard
done
- supplied
Work
Heat
==QQ−
Q
sr
s
=
1750 729
1750
−
= 0.5834 or 58.34%. (Ans.)
(iii)Mean effective pressure, pm :
Mean effective pressure is given by
pm = Work done per cycle
Stroke volume
or pm =^1
34 3 11
44 55 22 11
V
pV V pV pV pV pV
s
()−+ −
−
− −
−
L
N
M
O
Q
γγP
VVrVVVVV V
Vr V
c cc
sc
15 2 3 4
1
== == =
=−
,,,
()
ρ Q r
VV
V
V
V
Vr V
sc
c
s
c
sc
= + =+
∴=−
L
N
M
M
M
O
Q
P
P
P
1
() 1