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Carbon dioxide (CO2) at 1 bar, 300 K enters a
compressor operating at steady state and is compressed
adiabatically to an exit state of 10 bar, 540 K. The CO2
is modeled as an ideal gas, and kinetic and potential energy
effects are negligible.
For the compressor, determine:
(a) the work input, in kJ per kg of CO2 flowing,
(b) the rate of entropy production, in kJ/K per kg of
CO2 flowing, and
(c) the percent isentropic compressor efficiency.
Compressor inlet condition :
Temperature T1 = 300K
Pressure P1 = 1 bar
Compressor outlet condition :
T2 = 540 K
P2 = 10 bar
Assumptions : 1. Steady state process.
2. Negligible kinetic and potential energy changes.
3. Adiabatic process.
a) For compressor work input :
W = nYR(T1 - T2) /(Y-1)
Y - specific heat ratio for co2 = 1.28
Work input required per 1kg.
Moles n = 1000 gm/(44 gm/mol) = 22.72 mol
W = 22.72 mol*1.28*8.314J/mol.k * (300 - 540)/(1.28-1)
W = - 207243.79 J
W = -207.243 kJ
And this work is per kg of CO2 flowing, W = -207.243 kJ/kg
(-) sign shows work required for compression.
Ans: W = -207.243 kJ/kg
b) rate of production of entropy :
For compressor entropy change formula
(ΔS)system = Cpln(T2/T1) - Rln(P2/P1)
= 0.946 kj/kg.k * ln(540/300) - (8.314kJ/kmol.k)/44kg/kmol)*ln(10/1)
(ΔS)system = 0.556 - 0.435= 0.121 kJ/kg.k
Change in entropy (ΔS)system = 0.121 kJ/kg.k
compressor is insulated then no heat transfer Q = 0
Entropy change for surrounding( ΔS)surr = Q/Tsurr = 0
Total entropy generation,
(ΔS)gen = ΔS)system + ΔS)surr = 0.121 + 0 = 0.121 kJ/k.kg
Ans : 0.121 kJ/kg.k
c) isentropic compressor efficiency :
=( isentropic work input/real work input)*100
=[ (T1 - T2isent) /(T1 - T2)]*100
By isentropic process,
T2isent = T1*(P2/P1)^(Y-1)/Y
= 300*(10/1)^(1.28-1)/1.28
= 496.44 K
T2isent = 496.44 K
Wisent = YnR(T1 - T2isent) /(Y-1)
= 1.28*22.72*8.314*(300 - 496.44)/(1.28-1)
= 169633.47 J
= 169.633 kJ
isentropic efficiency = (169.633)/(207.243)*100
= 81.85%
or
isentropic efficiency =[ (300- 496.44)/(300-540)]*100= 81.85%
Ans : 81.85%