
Separate control volumes around compressor and nozzle. For ideal compressor we have inlet : 1 and exit : 2
Adiabatic : q = 0.
Reversible: sgen = 0
Energy Eq. h1 + 0 = wC + h2;
Entropy Eq : s1 + 0/T + 0 = s2 - wC
= h2 - h1 , s2 = s1
Propertiesair: CPo = 1.004 kJ/kg K, R = 0.287 kJ/kg K, k = 1.4
Process gives constant s (isentropic) which with constant CPo gives

The ideal nozzle then expands back down to P1 (constant s) so state 3 equals state 1. The energy equation has no work but kinetic energy and gives:
