Low frontal area
Higher thrust
High pressure rise
None of these
A. Low frontal area
1 : 1
2 : 1
4 : 1
1 : 6
Compressor efficiency
Isothermal efficiency
Volumetric efficiency
Mechanical efficiency
Centrifugal type
Reciprocating type
Lobe type
Axial flow type
Lower at low speed
Higher at high altitudes
Same at all altitudes
Higher at high speed
75 %
85 %
90 %
99 %
p₂ = (p₁ + p₃)/2
p₂ = p₁. p₃
P₂ = Pa × p₃/p₁
p₂ = Pa p₃/p₁
Ideal compression
Adiabatic compression
Isentropic compression
Isothermal compression
Compression ratio
Expansion ratio
Compressor efficiency
Volumetric efficiency
Compressor efficiency
Volumetric efficiency
Isothermal efficiency
Mechanical efficiency
Actual volume of the air delivered by the compressor when reduced to normal temperature and pressure conditions
Volume of air delivered by the compressor
Volume of air sucked by the compressor during its suction stroke
None of the above
Equal to
Less than
Greater than
None of these
Atmospheric conditions at any specific location
20°C and 1 kg/cm² and relative humidity 36%
0°C and standard atmospheric conditions
15°C and 1 kg/cm²
Reciprocating compressor
Centrifugal compressor
Axial flow compressor
Turbo compressor
Equal to
Less than
More than
None of these
Before the intercooler
After the intercooler
Between the aftercooler and receiver
Before first stage suction
Jet velocity
Twice the jet velocity
Half the jet velocity
Average of the jet velocity
Compressor efficiency
Isentropic efficiency
Euler's efficiency
Pressure coefficient
0.5 kg
1.0 kg
1.3 kg
2.2 kg
Lower power consumption per unit of air delivered
Higher volumetric efficiency
Decreased discharge temperature
All of the above
Large discharge at high pressure
Low discharge at high pressure
Large discharge at low pressure
Low discharge at low pressure
Carbonisation of coal
Passing steam over incandescent coke
Passing air and a large amount of steam over waste coal at about 65°C
Partial combustion of coal, coke, anthracite coal or charcoal in a mixed air steam blast
200°C
500°C
700°C
1000°C
More
Less
Same
Depends on other factors
Surrounding air
Compressed atmospheric air
Its own oxygen
None of these
Increase in net output but decrease in thermal efficiency
Increase in thermal efficiency but decrease in net output
Increase in both thermal efficiency and net output
Decrease in both thermal efficiency and net output
Net work output and heat supplied
Net work output and work done by turbine
Actual heat drop and isentropic heat drop
Net work output and isentropic heat drop
Rise gradually towards the point of use
Drop gradually towards the point of use
Be laid vertically
Be laid exactly horizontally
Compressor pressure ratio
Highest pressure to exhaust pressure
Inlet pressure to exhaust pressure
Pressures across the turbine
Increases
Decreases
Remain same
First increases and then decreases
Centrifugal compressors deliver practically constant pressure over a considerable range of capacities
Axial flow compressors have a substantially constant delivery at variable pressures
Centrifugal compressors have a wider stable operating range than axial flow compressors
Axial flow compressors are bigger in diameter compared to centrifugal type