p₂/p₁ = p₃/p₂
p₁/p₃ = p₂/p₁
p₁ = p₃
p₁ = p₂ p₃
A. p₂/p₁ = p₃/p₂
Ammonia and water vapour
Carbon dioxide
Nitrogen
Hydrogen
Mechanical efficiency
Volumetric efficiency
Isothermal efficiency
Adiabatic efficiency
Free air delivery
Compressor capacity
Swept volume
None of these
Reduction of speed of incoming air and conversion of part of it into pressure energy
Compression of inlet air
Increasing speed of incoming air
Lost work
Standard air
Free air
Compressed air
Compressed air at delivery pressure
Increases
Decreases
Remains same
Increases/decreases depending on compressor capacity
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, eke, anthracite coal or charcoal in a mixed air steam blast
Increases
Decreases
Remain same
First increases and then decreases
Isothermal compression
Isentropic compression
Polytropic compression
None of these
Increases thermal efficiency
Allows high compression ratio
Decreases heat loss is exhaust
Allows operation at very high altitudes
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
Atmospheric
Slightly more than atmospheric
Slightly less than atmospheric
Pressure slightly less than atmospheric and temperature slightly more than atmospheric
Reduced
Increased
Zero
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
Increase velocity
Make the flow streamline
Convert pressure energy into kinetic energy
Convert kinetic energy into pressure energy
The compression ratio in each stage should be same
The intercooling should be perfect
The workdone in each stage should be same
All of the above
r -1
1 - r -1
1 - (1/r) -1/
1 - (1/r) /-1
More
Less
Same
Depends on other factors
Centrifugal type
Reciprocating type
Lobe type
Axial flow type
Stainless steel
High alloy steel
Duralumin
Timken, Haste alloys
Pressure ratio
Pressure coefficient
Degree of reaction
Slip factor
D₁/D₂ = (p₁ p₃)1/2
D₁/D₂ = (p₁/p₃)1/4
D₁/D₂ = (p₁ p₃)1/4
D₁/D₂ = (p₃/p₁)1/4
No propeller
Propeller in front
Propeller at back
Propeller on the top
(v₁² -v₂²)/2g
(v₁ - v₂)²/2g
(v₁² -v₂²)/g
(v₁ - v₂)²/g
Exit nozzle, which is a constant volume process
Exit nozzle, which is essentially an isentropic process
Turbine blades, which is a constant volume process
Turbine blades, which is essentially an isentropic process
Compressor efficiency
Isentropic efficiency
Euler's efficiency
Pressure coefficient
0.1 %
0.5 %
1 %
5 %
p₂ = p₁ × p₃
p₂ = p₁/p₃
p₂ = p₁ × p₂
p₂ = p₃/p₁
No flow of air
Fixed mass flow rate regardless of pressure ratio
Reducing mass flow rate with increase in pressure ratio
Increased inclination of chord with air steam
Compression ratio
Expansion ratio
Compressor efficiency
Volumetric efficiency