Of cooling medium
Of freezing zone
Of evaporator
At which refrigerant gas becomes liquid
D. At which refrigerant gas becomes liquid
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
1 m3 of water
1 m3 of dry air
1 kg of wet air
1 kg of dry air
1
1.25
2.15
5.12
Increases C.O.P
Decreases C.O.P
C.O.P remains unaltered
Other factors decide C.O.P
Raise the pressure of the refrigerant
Raise the temperature of the refrigerant
Circulate the refrigerant through the refrigerating system
All of the above
Decreases
Increases
Remain same
Depends on other factors
Wet bulb temperature
Relative humidity
Dry bulb temperature
Specific humidity
25°C DBT and 100% RH
20°C DBT and 80% RH
22°C DBT and 60% RH
25°C DBT and 40% RH
Remains constant
Increases
Decreases
None of these
Low weight per tonne of refrigeration
High heat transfer rate
Low temperature at high altitudes
Higher coefficient of performance
Same
Less
More
None of these
1/4
1/3
3
4
After passing through the condenser
Before passing through the condenser
After passing through the expansion or throttle valve
Before entering the expansion valve
Compressor and condenser
Condenser and receiver
Receiver and evaporator
Evaporator and compressor
1 : 1
1 : 9
9 : 1
1 : 3
Remains constant
Increases
Decreases
None of these
Ammonia
Carbon dioxide
Sulphur dioxide
Fluorine
Does not alter C.O.P.
Increases C.O.P.
Decreases C.O.P.
None of these
Removes heat from a low temperature body and delivers it to a high temperature body
Removes heat from a high temperature body and delivers it to a low temperature body
Rejects energy to a low temperature body
None of the above
Temperature of medium being cooled must be below that of the evaporator
Refrigerant leaves the condenser as liquid
All solar thermally operated absorption systems are capable only of intermittent operation
Frost on evaporator reduces heat transfer
Remains constant
Increases
Decreases
None of these
Equalise
Reduce
Increase
None of these
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
Carnot cycle
Rankines cycle
Reversed Carnot cycle
None of the above
210 kJ/ min
21 kJ/ min
420 kJ/ min
840 kJ/ min
Gives noisy operation
Gives quiet operation
Requires little power consumption
Cools below 0°C
Halide torch
Sulphur sticks
Soap and water
All of these
A gas will never liquefy
A gas will immediately liquefy
Water will evaporate
Water will never evaporate
Ammonia
R-12
Sulphur dioxide
Carbon dioxide
Degree of superheat at exit from the evaporator
Temperature of the evaporator
Pressure in the evaporator
None of the above