Isentropic compression
Isothermal compression
Polytropic compression
None of the above
A. Isentropic compression
Compressor work and turbine work
Output and input
Actual total head temperature drop to the isentropic total head drop from total head inlet to static head outlet
Actual compressor work and theoretical compressor work
Control temperature
Control output of turbine
Control fire hazards
Increase efficiency
Centrifugal type
Axial flow type
Radial flow type
None of these
Air stream blocking the passage
Motion of air at sonic velocity
Unsteady, periodic and reversed flow
Air stream not able to follow the blade contour
Same
Less
More
None of these
Equal to
Less than
More than
None of these
Increases as clearance volume increases
Decreases as clearance volume increases
Is independent of clearance volume
Increases as clearance volume decreases
Decreases
Increases
Does not change
None of these
Reciprocating compressor
Centrifugal compressor
Axial flow compressor
Turbo compressor
Mechanical efficiency
Volumetric efficiency
Isothermal efficiency
Adiabatic efficiency
Higher
Lower
Same
None of the above
Standard air
Free air
Compressed air
Compressed air at delivery pressure
Isothermal h.p. to the BHP of motor
Isothermal h.p. to adiabatic h.p.
Power to drive compressor to isothermal h.p.
Work to compress air isothermally to work for actual compression
Has no effect on
Decreases
Increases
None of these
One air stream
Two or more air streams
No air stream
Solid fuel firing
These are used to dampen pulsations
These act as reservoir to take care of sudden demands
These increase compressor efficiency
These knock out some oil and moisture
Work factor
Slip factor
Degree of reaction
Pressure coefficient
Centrifugal compressor
Axial compressor
Pumps
All of the above
3.5 : 1
5 : 1
8 : 1
12 : 1
Power consumption per unit of air delivered is low
Volumetric efficiency is high
It is best suited for compression ratios around 7:1
The moisture in air is condensed in the intercooler
Isothermal compression
Isentropic compression
Polytropic compression
None of these
Rise gradually towards the point of use
Drop gradually towards the point of use
Be laid vertically
Be laid exactly horizontally
0.1 bar and 20°C
1 bar and 20°C
0.1 bar and 40°C
1 bar and 40°C
As large as possible
As small as possible
About 50% of swept volume
About 100% of swept volume
6000 KW
15 KW
600 KW
150 KW
Free air delivery
Compressor capacity
Swept volume
None of these
Forward curved
Backward curved
Radial
None of these
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
Isothermally
Polytropically
Isentropically
None of these
10 bar
20 bar
30 bar
50 bar