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A cascade refrigeration system of 100 tons (350 kW) capacity uses ammonia and carbon dioxide the evaporating and condensing temperatures of CO2 are         –40°C and 5°C, respectively. The evaporating temperature of NH3 is –7°C. The power supplied to the ammonia compressor is 96.5 kW. In the CO2 circuit, the liquid leaving the condenser is saturated, the vapor leaving the evaporator is dry and saturated, and compression is isentropic. Calculate the mass flow rate of CO2 and the C.O.P of the system. The following data for CO2 may be used:

Temperature

°C

Pressure,

bars

Enthalpy, kJ/kg

Entropy,

kJ/kg K

 

 

Liquid

Vapor

Liquid

Vapor

–40

10.05

332.7

652.8

3.8531

5.2262

5

39.70

43.10

649.8

4.2231

5.0097

Specific heat of superheated vapor            cp = 0.85 kJ/kg K.

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