Horizontal line
Vertical line
Inclined line
Curved line
B. Vertical line
Liquid
Sub-cooled liquid
Saturated liquid
Wet vapour
Ammonia
Carbon dioxide
Sulphur dioxide
R-12
Water and hydrogen
Ammonia and hydrogen
Ammonia, water and hydrogen
None of these
Remains constant
Increases
Decreases
None of these
B.P.F. - 1
1 - B.P.F.
1/ B.P.F.
1 + B.P.F.
Ineffective refrigeration
High power consumption
Freezing automatic regulating valve
Corrosion of whole system
Remains constant
Increases
Decreases
None of these
Absolute
Relative
Specific
None of these
(td₁ -td₃)/( td₂ -td₃)
(td₂ -td₃)/( td₁ -td₃)
(td₃ -td₁)/( td₂ -td₃)
(td₃ -td₂)/( td₁ -td₃)
Suction pressure
Discharge pressure
Critical pressure
Back pressure
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
1.25
0.8
0.5
0.25
Increases C.O.P
Decreases C.O.P
C.O.P remains unaltered
Other factors decide C.O.P
Evaporator
Safety relief valve
Dehumidifier
Driers
1
1.25
2.15
5.12
Decrease in fin spacing and increase in number of rows
Increase in fin spacing and increase in number of rows
Increase in fin spacing and decrease in number of rows
Decrease in fin spacing and decrease in number of rows
Same
More
Less
More/less depending on rating
Liquid pump
Generator
Absorber and generator
Absorber, generator and liquid pump
Less than 2 kg
More than or equal to 3.65 kg
More than 10 kg
There is no such consideration
Heat supplied by the gas burner to the heat absorbed by the evaporator
Heat absorbed by the evaporator to the heat supplied by the gas burner
Heat supplied by the gas burner minus the heat absorbed by the evaporator to the heat supplied by the gas burner
Heat absorbed by the evaporator minus the heat supplied by the gas burner to the heat absorbed by the evaporator
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
Condenser
Evaporator
Absorber
Condenser, absorber and separator (rectifier)
Small displacements and low condensing pressures
Large displacements and high condensing pressures
Small displacements and high condensing pressures
Large displacements and low condensing pressures
Cooled and humidified
Cooled and dehumidified
Heated and humidified
Heated and dehumidified
Strong solution to weak solution
Weak solution to strong solution
Strong solution to ammonia vapour
Ammonia vapours to weak solution
Critical pressure of refrigerant
Much below critical pressure
Much above critical pressure
Near critical pressure
20°C DBT and 50% RH
26°C DBT and 50% RH
20°C DBT and 60% RH
26°C DBT and 60% RH
Compression
Expansion
Condensation
Evaporation
Lack of cooling water
Water temperature being high
Dirty condenser surface
All of these
More
Less
Equally
Unpredictable