298 POWER PLANT ENGINEERING
p 2 =1.01 × 6 = 6.06 bar
Rp =^2
1
P
p
= 6
Pressure at point 4 = 6.06 – 0.15 = 5.91 bar
Applying isentropic law to the process 1 – 2
T 2 ′ = T 1 (RP)(γ – 1)/γ = 288(6)0.286 = 480 K
ηc =^21
21
(T T )
(T T )
′−
−
But T 2 = T 1 + ηc (T 2 ′ – T 1 ) = 288 + 0.8(480 – 288) = 528 K
p 3 = 6.06 – 0.15 = 5.91 bar
and p 4 = 1.01 + 0.15 = 1.16 bar
Applying isentropic law to the process 4 – 5′
T 5 ′ = (1)/^4
3
4
T
P
P
γ− γ
= 0.286
(700 273)
5.91
1.16
+
= 612 K
ηt =^45
45
(T T )
(T T )′
−
−
or, T 5 = T 4 – ηt(T 4 – T 5 ′)
= 973 – 0.85(973 – 612) = 666 K
The effectiveness of the regenerator is given by
ε =^45
45
(T T )
(T T )
−
−
T 3 = T 2 + 0.75 (T 5 – T 2 ) = 528 + 0.75(666 – 528) = 631.5 kW
Wc = Cp(T 2 – T 1 ) = 1 × (528 – 288) = 240 kJ/kg
Wt = Cp(T 4 – T 5 ) = 1 × (973 – 666) = 307 kJ/kg
Wn = Wt – Wc = 307 – 240 = 67 kJ/kg
QS = Cp(T 4 – T 3 ) = 1 × (973 – 631.5) = 341.5 kJ/kg
ηth =
W
Q
n
s
=
67
341.5
= 0.196 = 19.6%.
Example 2. In a constant pressure open cycle gas turbine air enters at 1 bar and 20°C and
leaves the compressor at 5 bar. Using the following data; Temperature of gases entering the turbine
= 680°C, pressure loss in the combustion chamber = 0.1 bar, ηcompressor = 85%, ηturbine = 80%, ηcombustion
= 85%, γ = 1.4 and cp = 1.024 kJ/kgK for air and gas, find:
(1) The quantity of air circulation if the plant develops 1065 kW.