At compressor inlet
temperature T1 = 20∘C + 273 = 293 K
Maximum cycle temperature
T4 = 865°C + 273 = 1138 K
Compression ratio
p2/p1= 7.8
Gas constants R = 0.287 KJ/kg.k
Specific heat capacity of air at constant pressure
cp=1.005KJ/kg.k
Specific heat capacity of air at constant volume
cv=0.718KJ/kg.k
PV diagram
Process 1-2
isentropic compression
T2/T1=(p2/p1)^(k−1/K)
T2/293=(7.8)^(1.4−1/1.4)
T2=526.91 K
process 4-5
isentropic expansion:
T5/T4=(p5/p4)^(k−1/K)
T5/T4=(p1/p2)^(k−1/K)
T5/1138=(1/7.8)^(1.4−1/1.4)
T5 = 632.81 K
At state 3
T3=T5−10
T3=632.81−10 = 622.81 K
T5−T6=T3−T2
T6=T5−(T3−T2)
= 632.81 - (622.81 - 526.91)
= 536.91 K
Net work output
Wnet = Wt−Wc
Wnet = cp(T4−T5) − cp(T2−T1)
Wnet=1.005 kJ/kg-K x (1138−632.81)K − 1.005kJ/K x (526.91−293)K
Wnet = 272.63 kJ/kg
˙Wnet=˙mWnet
130 =˙m(272.63)
˙m=0.4768 Kg/sec
Heat added
˙Qin=˙mcp(T4−T3)
= 0.4768 kg/s x 1.005 kJ/kg-K x (1138 - 622.81)
= 246.88 kJ/s = 246.9 kW
Heat rejected
Qout=˙mcp(T6−T1)
˙Qout=(0.4768 kg/s) x (1.005 kJ/kg-K) x (536.91 - 293)K
= 116.88 kJ/s = 116.9 kW
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