After passing through the condenser
Before passing through the condenser
After passing through the expansion or throttle valve
Before entering the compressor
D. Before entering the compressor
Saturated liquid
Wet vapour
Dry saturated vapour
Superheated vapour
Decreases
Increases
Remain same
Depends on other factors
Domestic refrigerators
Commercial refrigerators
Air conditioning
Gas liquefaction
Zero
0.5
0.75
1.0
Low boiling point
High critical temperature
High latent heat of vaporisation
All of these
Ineffective refrigeration
High power consumption
Freezing automatic regulating valve
Corrosion of whole system
210 kJ/ min
21 kJ/ min
420 kJ/ min
840 kJ/ min
Compressor
Condenser
Evaporator
Expansion valve
Does not alter C.O.P.
Increases C.O.P.
Decreases C.O.P.
None of these
Same
Lower
Higher
None of these
Low weight per tonne of refrigeration
High heat transfer rate
Low temperature at high altitudes
Higher coefficient of performance
High sensible heat
High total heat
High latent heat
Low latent heat
Colourless
Odourless
Non-flammable
All of these
Ammonia
Carbon dioxide
Sulphur dioxide
R-12
Temperature, pressure and enthalpy
Specific volume and enthalpy
Temperature and enthalpy
Temperature, pressure, specific volume and enthalpy
Single fluid
Two fluids
Three fluids
None of these
Before entering the compressor
After leaving the compressor
Before entering the condenser
After leaving the condenser
Reversed Carnot cycle
Reversed Otto cycle
Reversed Joule cycle
Reversed Rankine cycle
T₁ / (T₂ - T₁)
(T₂ - T₁)/T₁
(T₁ - T₂)/T₁
T₂/ (T₂ - T₁)
Humidification
Dehumidification
Heating and humidification
Cooling and dehumidification
(td₂ - td₃)/(td₃ - td₁)
(td₃ - td₂)/(td₃ - td₁)
(td₃ - td₁)/(td₂ - td₃)
(td₃ - td₁)/(td₃ - td₂)
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
(hA - h2)/ (h1 - h2)
(h2 - hA)/ (h1 - h2)
(h1 - h2)/ (hA - h2)
(hA - h1)/ (h2 - h1)
50 kcal/ min
50 kcal/ hr
80 kcal/ min
80 kcal/ hr
0.2
1.2
5
6
20 to 50°C
50 to 70°C
70 to 110°C
None of these
Will be higher
Will be lower
Will remain unaffected
May be higher or lower depending upon the nature of noncondensable gases
Actual COP/theoretical COP
Theoretical COP/actual COP
Actual COP × theoretical COP
None of these
Automatic expansion valve
High side float valve
Thermostatic expansion valve
Low side float valve
Brass
Copper
Steel
Aluminium