EXAMPLE 4.29 Suppose a 100 ton cooling capacity ammonia refrigeration plant is working at evaporating temperature -20°C and condensing temperature 34°C. The liquid is subcooled to 28°C in order to reduce the formation of flash gases. Ammonia vapour leaves the evaporator and enters the compressor at -6°C. There is a pressure loss of 0.1 bar at the suction valve and 0.5 bar at the discharge valves. Assume isentropic compression and take the volumetric efficiency of the compressor to be 80%. Determine the following quantities: (a) Refrigerating effect per kg (b) Mass flow rate in kg/min (c) Piston displacement in m/min (d) COP of the plant (e) Power required (kW)

Elements Of Electromagnetics
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Author:Sadiku, Matthew N. O.
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EXAMPLE 4.29 Suppose a 100 ton cooling capacity ammonia refrigeration plant is working
at evaporating temperature -20°C and condensing temperature 34°C. The liquid is subcooled to
28°C in order to reduce the formation of flash gases. Ammonia vapour leaves the evaporator and
enters the compressor at -6°C. There is a pressure loss of 0.1 bar at the suction valve and 0.5
bar at the discharge valves. Assume isentropic compression and take the volumetric efficiency
of the compressor to be 80%.
Determine the following quantities:
(a) Refrigerating effect per kg
(b) Mass flow rate in kg/min
(c) Piston displacement in m/min
(d) COP of the plant
(e) Power required (kW)
Transcribed Image Text:EXAMPLE 4.29 Suppose a 100 ton cooling capacity ammonia refrigeration plant is working at evaporating temperature -20°C and condensing temperature 34°C. The liquid is subcooled to 28°C in order to reduce the formation of flash gases. Ammonia vapour leaves the evaporator and enters the compressor at -6°C. There is a pressure loss of 0.1 bar at the suction valve and 0.5 bar at the discharge valves. Assume isentropic compression and take the volumetric efficiency of the compressor to be 80%. Determine the following quantities: (a) Refrigerating effect per kg (b) Mass flow rate in kg/min (c) Piston displacement in m/min (d) COP of the plant (e) Power required (kW)
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