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
B. Volume of air delivered by the compressor
Inlet whirl velocity
Outlet whirl velocity
Inlet velocity of flow
Outlet velocity of flow
Same
Less
More
None of these
Increase temperature
Reduce turbine size
Increase power output
Increase speed
To accommodate Valves in the cylinder head
To provide cushioning effect
To attain high volumetric efficiency
To provide cushioning effect and also to avoid mechanical bang of piston with cylinder head
At very high speed
At very slow speed
At average speed
At zero speed
Ideal compression
Adiabatic compression
Isentropic compression
Isothermal compression
Reciprocating compressor
Centrifugal compressor
Axial flow compressor
Turbo compressor
Zero
Less
More
Same
Compressor efficiency
Isothermal efficiency
Volumetric efficiency
Mechanical efficiency
6000 KW
15 KW
600 KW
150 KW
p₂ = (p₁ + p₃)/2
p₂ = p₁. p₃
P₂ = Pa × p₃/p₁
p₂ = Pa p₃/p₁
Low frontal area
Higher thrust
High pressure rise
None of these
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
Mechanical efficiency
Volumetric efficiency
Isothermal efficiency
Adiabatic efficiency
Injecting water into the compressor
Burning fuel after gas turbine
Injecting ammonia into the combustion chamber
All of the above
Isentropic compression
Isothermal compression
Polytropic compression
None of the above
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
Multistage compression
Cold water spray
Both (A) and (B) above
Fully insulating the cylinder
In two phases
In three phases
In a single phase
In the form of air and water mixture
0.5 kg
1.0 kg
1.3 kg
2.2 kg
0.2
0.3
0.4
0.5
2 : 1
4 :1
61 : 1
9 : 1
W₁/(W₁ + W₂)
W₂/(W₁ + W₂)
(W₁ + W₂)/W₁
(W₁ + W₂)/W₂
1 bar
16 bar
64 bar
256 bar
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
Radial flow compressors
Axial flow compressors
Pumps
All of these
Standard air
Free air
Compressed air
Compressed air at delivery pressure
Same
More
Less
Depends on other factors
Gauge discharge pressure to the gauge intake pressure
Absolute discharge pressure to the absolute intake pressure
Pressures at discharge and suction corresponding to same temperature
Stroke volume and clearance volume
Increase
Decrease
Remain same
May increase or decrease depending on clearance volume