Air flow rate through the compressor, m = 0.5 kg/s
Velocity of air at the inlet to compressor, C1 = 6 m/s
Velocity of air at the outlet of compressor, C2 = 5 m/s
Pressure of air at the inlet to the compressor, p1 = 1 bar
Pressure of air at outlet to the compressor, p2 = 7 bar
Specific volume of air at inlet to the compressor, v1 = 0.85 m3/kg
Specific volume of air at outlet to the compressor, v2 = 0.16 m3/kg
Difference of internal energy at the outlet and inlet of the compressor
(u2 – u1) = 90 kJ/kg
Heat rejected by air (to cooling water),
Q = – \(\cfrac{60}{0.5}\) = – 120 kJ/kg.
(i) Power required to drive the compressor :
Using the steady flow energy equation,
(Note that the change in kinetic energy is negligibly small in comparison with the other terms).
Work input required = 237 kJ/kg = 237 × 0.5 kJ/s = 118.5 kW
Hence, power required to drive the compressor = 118.5 kW.
(ii) Inlet and outlet pipe cross-sectional areas, A1 and A2 :
Using the relation,
Inlet pipe cross-sectional area, A1 = 0.0708 m2.
Again,
Outlet pipe cross-sectional area, A2 = 0.016 m2.