168 ENGINEERING THERMODYNAMICS
dharm
/M-therm/Th4-4.pm5
Pressure of air at outlet to the compressor, p 2 = 7 bar
Specific volume of air at inlet to the compressor, v 1 = 0.85 m^3 /kg
Specific volume of air at outlet to the compressor, v 2 = 0.16 m^3 /kg
Difference of internal energy at the outlet and inlet of the compressor,
(u 2 – u 1 ) = 90 kJ/kg
Heat rejected by air (to cooling water),
Q = –
60
0.5 = – 120 kJ/kg.
(i)Power required to drive the compressor :
Using the steady flow energy equation,
u 1 + C^1
2
2 + p^1 v^1 + Q = u^2 +
C 22
2 + p^2 v^2 + W
∴ W = (u 1 – u 2 ) +
CC 12 22
22 −
F
HG
I
KJ + (p^1 v^1 – p^2 v^2 ) + Q
= – 90 +
1
1000
6
2
5
2
22
−
F
HG
I
KJ +
10
1000
5
(1 × 0.85 – 7 × 0.16) + (– 120)
= – 90 + 0.0055 – 27 – 120 = – 237 kJ/kg (app.).
(Note that the change in kinetic energy is negligibly small in comparison with the other
terms).
i.e., Work input required = 237 kJ/kg = 237 × 0.5 kJ/s = 118.5 kW
Hence, power required to drive the compressor = 118.5 kW. (Ans.)
(ii)Inlet and outlet pipe cross-sectional areas, A 1 and A 2 :
Using the relation,
m& CA
v
=
∴ A 1 = mv&
C
1
1
00
6
= .5× .85m^2 = 0.0708 m^2
i.e., Inlet pipe cross-sectional area, A 1 = 0.0708 m^2. (Ans.)
Again, A 2 = mv&
C
2
2
00
5
= .5× .16m^2 = 0.016 m^2.
i.e., Outlet pipe cross-sectional area, A 2 = 0.016 m^2. (Ans.)
Note. In this example, the steady flow energy equation has been used, despite the fact the compression
consists of : suction of air ; compression in a closed cylinder ; and discharge of air. The steady flow equation can be
used because the cycle of processes takes place many times in a minute, and therefore, average effect is steady flow
of air through the machine.
Example 4.38. In a steam plant, 1 kg of water per second is supplied to the boiler. The
enthalpy and velocity of water entering the boiler are 800 kJ/kg and 5 m/s. The water receives
2200 kJ/kg of heat in the boiler at constant pressure. The steam after passing through the turbine
comes out with a velocity of 50 m/s, and its enthalpy is 2520 kJ/kg. The inlet is 4 m above the
turbine exit. Assuming the heat losses from the boiler and the turbine to the surroundings are