(hA - h2)/ (h1 - h2)
(h2 - hA)/ (h1 - h2)
(h1 - h2)/ (hA - h2)
(hA - h1)/ (h2 - h1)
A. (hA - h2)/ (h1 - h2)
(C.O.P.)P = (C.O.P.)R + 2
(C.O.P.)P = (C.O.P.)R + 1
(C.O.P)P = (C.O.P)R - 1
(C.O.P)P = (C.O.P)R
Remains constant
Increases
Decreases
None of these
Suction pressure
Discharge pressure
Critical pressure
Back pressure
1 m3 of water
1 m3 of dry air
1 kg of wet air
1 kg of dry air
Dry bulb temperature
Wet bulb temperature
Dew point temperature
Relative humidity
Compressor
Condenser
Expansion valve
Evaporator
Simple air cooling system
Simple evaporative air cooling system
Bootstrap air cooling system
All of these
One cooling turbine and one heat exchanger
One cooling turbine and two heat exchangers
Two cooling turbines and one heat exchanger
Two cooling turbines and two heat exchangers
Carnot cycle
Rankines cycle
Reversed Carnot cycle
None of the above
Ammonia
Carbon dioxide
Sulphur dioxide
R-12
Which lies between the dry bulb and wet bulb temperatures of the incoming stream
Which lies between the wet bulb and dew point temperatures of the incoming stream
Which is lower than the dew point temperature of the incoming stream
Of adiabatic saturation of incoming stream
Horizontal line
Vertical line
Inclined line
Curved line
Critical pressure of refrigerant
Much below critical pressure
Much above critical pressure
Near critical pressure
Dry bulb temperature
Wet bulb temperature
Dew point temperature
Specific humidity
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 wet air
1 m3 of dry air
1 kg of wet air
1 kg of dry air
Vertical and uniformly spaced
Horizontal and uniformly spaced
Horizontal and non-uniformly spaced
Curved lines
Saturated liquid
Wet vapour
Dry saturated vapour
Superheated vapour
Low weight per tonne of refrigeration
High heat transfer rate
Low temperature at high altitudes
Higher coefficient of performance
Increase
Decrease
Remain unaffected
May increase or decrease depending on the type of refrigerant used
Remains constant
Increases
Decreases
None of these
Of cooling medium
Of freezing zone
Of evaporator
At which refrigerant gas becomes liquid
0.2
1.2
5
6
Circulating more quantity of cooling water through the condenser
Using water colder than the main circulating water
Employing a heat exchanger
Any one of the above
Dry bulb depression
Wet bulb depression
Dew point depression
Degree of saturation
Results in loss of heat due to poor heat transfer
Increases heat transfer rate
Is immaterial
Can be avoided by proper design
5°C
10°C
15°C
20°C
Humidity ratio
Relative humidity
Absolute humidity
Degree of saturation
1
1.25
2.15
5.12
Wet vapour region
Superheated vapour region
Sub-cooled liquid region
None of these