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Refrigeration Cycles Prof. U.S.P. Shet , Prof. T. Sundararajan and Prof. J.M . Mallikarjuna
Indian Institute of Technology Madras
6.3 Air Refrigeration System And Bell-Coleman Cycle Or
Reversed Brayton Cycle:
5
qc
H.E
Expander
Evaporator
Compressor
3
26
qe
Motor
6.3 (a) Air refrigeration system
P
V
1
4
5 3p2
6 2p1
6.3 (b) Air refrigeration system
Refrigeration Cycles Prof. U.S.P. Shet , Prof. T. Sundararajan and Prof. J.M . Mallikarjuna
Indian Institute of Technology Madras
T
S
1
2
5
3
p2
p1
6.3 (c) Air refrigeration system
The components of the air refrigeration system are shown in Fig.6.3(a). In this system,
air is taken into the compressor from atmosphere and compressed. The hot
compressed air is cooled in heat exchanger upto the atmospheric temperature (in ideal
conditions). The cooled air is then expanded in an expander. The temperature of the air
coming out from the expander is below the atmospheric temperature due to isentropic
expansion. The low temperature air coming out from the expander enters into the
evaporator and absorbs the heat. The cycle is repeated again. The working of air-
refrigeration cycle is represented on p-v and T-s diagrams in Fig.6.3(b) and (c).
Process 1-2 represents the suction of air into the compressor. Process 2-3 represents
the isentropic compression of air by the compressor. Process 3-5 represents the
discharge of high pressure air from the compressor into the heat exchanger. The
reduction in volume of air from v3 to v5 is due to the cooling of air in the heat exchanger.
Process 5-6 represents the isentropic expansion of air in the expander. Process 6-2
represents the absorption of heat from the evaporator at constant pressure.
Refrigeration Cycles Prof. U.S.P. Shet , Prof. T. Sundararajan and Prof. J.M . Mallikarjuna
Indian Institute of Technology Madras
6.3.1. Analysis of Bell-Coleman Cycle:
The air refrigeration system works on Bell-Coleman cycle.
Assumptions:
1) The compression and expansion processes are reversible adiabatic
processes.
2) There is a perfect inter-cooling in the heat exchanger.
3) There are no pressure losses in the system.
Net refrigeration effect
COP
Net work supplied
=
Work done per kg of air for the isentropic compression process 2-3 is given by,
C p 3 2W C (T - T )=
Work developed per kg of air for the isentropic expansion process 5-6 is given by,
E p 5 6W C (T - T )=
net C ENet work required W (W - W )= = p 3 2 p 5 6C (T - T ) - C (T - T )=
Net refrigerating effect per kg of air is given by,
net p 2 6R C (T - T )=
{ }
p 2 6net
net p 3 2 5 6
C (T - T )R
COP
W C (T - T ) - (T - T )
= =
For perfect inter-cooling, the required condition is T5 = T2
2 6
3 2 2 6
(T - T )
COP
(T - T ) - (T - T )
=
Refrigeration Cycles Prof. U.S.P. Shet , Prof. T. Sundararajan and Prof. J.M . Mallikarjuna
Indian Institute of Technology Madras
( )
( )
3 2
2 6
1
(forisentropic process)
T - T
- 1
T - T
=
3 2 3
2 6 2
1
T (1 - T / T )
- 1
T (1 - T / T )
=
For isentropic compression process 2-3 and for expansion process 5-6, we have,
-1 -1
3 51 2
2 2 6 1
T TP P
and
T P T P
γ γ
γ γ⎛ ⎞ ⎛ ⎞
= =⎜ ⎟ ⎜ ⎟
⎝ ⎠ ⎝ ⎠
Therefore, 3 5 6 2
5 2
2 6 5 3
T T T T
= or = (T = T )
T T T T
Q
2
3 2
T
COP
T - T
=
Advantages:
a) Air is a cheaper refrigerant and available easily compared to other
refrigerants.
b) There is no danger of fire or toxic effects due to leakage.
c) The total weight of the system per ton of refrigerating capacity is less.
Disadvantages:
(a) The quantity of air required per ton refrigerating capacity is far greater than
other systems.
(b) The COP is low and hence maintenance cost is high.
(c) The danger of frosting at the expander valves is more as the air taken into the
system always contains moisture.
Refrigeration Cycles Prof. U.S.P. Shet , Prof. T. Sundararajan and Prof. J.M . Mallikarjuna
Indian Institute of Technology Madras
Work done during Compression and Expansion Processes (for
polytropic processes) (Refer P-V-diagram) (For problem solving)
3 3 2 2
C 3 3 2 2
P V - P V
W P V - P V
n -1
= +
( )
( )
( )
3 3 2 2
3 3 2 2
3 3 2 2
P V - P V
P V - P V
n - 1
n
P V - P V
n -1
= +
=

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4 reversed brayton_cycle

  • 1. Refrigeration Cycles Prof. U.S.P. Shet , Prof. T. Sundararajan and Prof. J.M . Mallikarjuna Indian Institute of Technology Madras 6.3 Air Refrigeration System And Bell-Coleman Cycle Or Reversed Brayton Cycle: 5 qc H.E Expander Evaporator Compressor 3 26 qe Motor 6.3 (a) Air refrigeration system P V 1 4 5 3p2 6 2p1 6.3 (b) Air refrigeration system
  • 2. Refrigeration Cycles Prof. U.S.P. Shet , Prof. T. Sundararajan and Prof. J.M . Mallikarjuna Indian Institute of Technology Madras T S 1 2 5 3 p2 p1 6.3 (c) Air refrigeration system The components of the air refrigeration system are shown in Fig.6.3(a). In this system, air is taken into the compressor from atmosphere and compressed. The hot compressed air is cooled in heat exchanger upto the atmospheric temperature (in ideal conditions). The cooled air is then expanded in an expander. The temperature of the air coming out from the expander is below the atmospheric temperature due to isentropic expansion. The low temperature air coming out from the expander enters into the evaporator and absorbs the heat. The cycle is repeated again. The working of air- refrigeration cycle is represented on p-v and T-s diagrams in Fig.6.3(b) and (c). Process 1-2 represents the suction of air into the compressor. Process 2-3 represents the isentropic compression of air by the compressor. Process 3-5 represents the discharge of high pressure air from the compressor into the heat exchanger. The reduction in volume of air from v3 to v5 is due to the cooling of air in the heat exchanger. Process 5-6 represents the isentropic expansion of air in the expander. Process 6-2 represents the absorption of heat from the evaporator at constant pressure.
  • 3. Refrigeration Cycles Prof. U.S.P. Shet , Prof. T. Sundararajan and Prof. J.M . Mallikarjuna Indian Institute of Technology Madras 6.3.1. Analysis of Bell-Coleman Cycle: The air refrigeration system works on Bell-Coleman cycle. Assumptions: 1) The compression and expansion processes are reversible adiabatic processes. 2) There is a perfect inter-cooling in the heat exchanger. 3) There are no pressure losses in the system. Net refrigeration effect COP Net work supplied = Work done per kg of air for the isentropic compression process 2-3 is given by, C p 3 2W C (T - T )= Work developed per kg of air for the isentropic expansion process 5-6 is given by, E p 5 6W C (T - T )= net C ENet work required W (W - W )= = p 3 2 p 5 6C (T - T ) - C (T - T )= Net refrigerating effect per kg of air is given by, net p 2 6R C (T - T )= { } p 2 6net net p 3 2 5 6 C (T - T )R COP W C (T - T ) - (T - T ) = = For perfect inter-cooling, the required condition is T5 = T2 2 6 3 2 2 6 (T - T ) COP (T - T ) - (T - T ) =
  • 4. Refrigeration Cycles Prof. U.S.P. Shet , Prof. T. Sundararajan and Prof. J.M . Mallikarjuna Indian Institute of Technology Madras ( ) ( ) 3 2 2 6 1 (forisentropic process) T - T - 1 T - T = 3 2 3 2 6 2 1 T (1 - T / T ) - 1 T (1 - T / T ) = For isentropic compression process 2-3 and for expansion process 5-6, we have, -1 -1 3 51 2 2 2 6 1 T TP P and T P T P γ γ γ γ⎛ ⎞ ⎛ ⎞ = =⎜ ⎟ ⎜ ⎟ ⎝ ⎠ ⎝ ⎠ Therefore, 3 5 6 2 5 2 2 6 5 3 T T T T = or = (T = T ) T T T T Q 2 3 2 T COP T - T = Advantages: a) Air is a cheaper refrigerant and available easily compared to other refrigerants. b) There is no danger of fire or toxic effects due to leakage. c) The total weight of the system per ton of refrigerating capacity is less. Disadvantages: (a) The quantity of air required per ton refrigerating capacity is far greater than other systems. (b) The COP is low and hence maintenance cost is high. (c) The danger of frosting at the expander valves is more as the air taken into the system always contains moisture.
  • 5. Refrigeration Cycles Prof. U.S.P. Shet , Prof. T. Sundararajan and Prof. J.M . Mallikarjuna Indian Institute of Technology Madras Work done during Compression and Expansion Processes (for polytropic processes) (Refer P-V-diagram) (For problem solving) 3 3 2 2 C 3 3 2 2 P V - P V W P V - P V n -1 = + ( ) ( ) ( ) 3 3 2 2 3 3 2 2 3 3 2 2 P V - P V P V - P V n - 1 n P V - P V n -1 = + =