Compressor
Condenser
Expansion valve
Evaporator
A. Compressor
After passing through the condenser
Before passing through the condenser
After passing through the expansion or throttle valve
Before entering the expansion valve
Wet bulb temperature
Dry bulb temperature
Dew point temperature
None of these
Same
Lower
Higher
None of these
Ammonia is absorbed in hydrogen
Ammonia is absorbed in water
Ammonia evaporates in hydrogen
Hydrogen evaporates in ammonia
Water and hydrogen
Ammonia and hydrogen
Ammonia, water and hydrogen
None of these
Wet bulb temperature
Relative humidity
Dry bulb temperature
Specific humidity
Always less than unity
Always more than unity
Equal to unity
Any one of the above
Constant pressure valve
Constant temperature valve
Constant superheat valve
None of these
Same
More
Less
More or less depending on ambient conditions
Reversed Carnot cycle
Reversed Joule cycle
Reversed Brayton cycle
Reversed Otto cycle
In evaporator
Before expansion valve
Between compressor and condenser
Between condenser and evaporator
Water
Ammonia
Freon
Aqua-ammonia
Coefficient of performance of refrigeration
Coefficient of performance of heat pump
Relative coefficient of performance
Refrigerating efficiency
20 to 50°C
50 to 70°C
70 to 110°C
None of these
Freon-12
NH3
CO2
Freon-22
Reversed Carnot cycle
Reversed Otto cycle
Reversed Joule cycle
Reversed Rankine cycle
Receiver
Expansion valve
Evaporator
Compressor discharge
Carbon dioxide
Sulphur dioxide
Lithium bromide
R-12
Remains constant
Increases
Decreases
None of these
Does not alter C.O.P.
Increases C.O.P.
Decreases C.O.P.
None of these
Carnot cycle
Reversed Carnot cycle
Rankines cycle
Brayton cycle
Is less than 1
Is more than 1
Is equal to 1
Depends upon the make
Between the combustion chamber and the first heat exchanger
Between the first heat exchanger and the secondary compressor
Between the secondary compressor and the second heat exchanger
Between the second heat exchanger and the cooling turbine
The mass of water vapour present in 1 m3 of dry air
The mass of water vapour present in 1 kg of dry air
The ratio of the actual mass of water vapour in a unit mass of dry air to the mass of water vapour in the same mass of dry air when it is saturated at the same temperature and pressure.
The ratio of actual mass of water vapour in a given volume of moist air to the mass of water vapour in the same volume of saturated air at the same temperature and pressure
1 m3 of water
1 m3 of dry air
1 kg of wet air
1 kg of dry air
Dehumidification
Cooling and humidification
Cooling and dehumidification
Dehumidification and pure sensible cooling
Before entering the compressor
After leaving the compressor
Before entering the condenser
After leaving the condenser
B.P.F. - 1
1 - B. P.F.
1/ B.P.F.
1 + B.P.F.
0.1 to 0.5 h.p. per ton of refrigeration
0.5 to 0.8 h.p. per ton of refrigeration
1 to 2 h.p. per ton of refrigeration
2 to 5 h.p. per ton of refrigeration
Involves no change in volume
Takes place at constant temperature
Takes place at constant entropy
Takes place at constant pressure