The operating temperatures of a lithium bromide-water absorption system, as shown in Figure 5.1, are as follows: Generator Condenser 100°C 35°C Evaporator Absorber 10°C 30°C The mass flow raté delivered by the aqua pump is 0.5 kg/s. Calculate: (a) The heat supplied to the generator (b) The heat rejected at the condenser and absorber (c) The cooling produced by the evaporator (d) The coefficient of performance of the cycle.
The operating temperatures of a lithium bromide-water absorption system, as shown in Figure 5.1, are as follows: Generator Condenser 100°C 35°C Evaporator Absorber 10°C 30°C The mass flow raté delivered by the aqua pump is 0.5 kg/s. Calculate: (a) The heat supplied to the generator (b) The heat rejected at the condenser and absorber (c) The cooling produced by the evaporator (d) The coefficient of performance of the cycle.
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Transcribed Image Text:5.5 The operating temperatures of a lithium bromide-water absorption system, as shown in
Figure 5.1, are as follows:
Generator
Condenser
100°C
35°C
Evaporator
Absorber
10°C
30°C
The mass flow rate delivered by the aqua pump is 0.5 kg/s. Calculate:
(a) The heat supplied to the generator
(b) The heat rejected at the condenser and absorber
(c)
The cooling produced by the evaporator
(d) The coefficient of performance of the cycle.
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