Degree of super-saturation
Degree of superheat
Degree of under-cooling
None of these
C. Degree of under-cooling
The steam is expanded in nozzles only and there is a pressure drop and heat drop
The steam is expanded both in fixed and moving blades continuously
The steam is expanded in moving blades only
The pressure and temperature of steam remains constant
Provide air around burners for obtaining optimum combustion
Transport and dry the coal
Convert CO (formed in lower zone of furnace) into CO₂ at higher zone
Air delivered by forced draft fan
No drum
One drum
Two drums
Three drums
There is no pressure drop due to condensation
Steam is admitted at boiler pressure and exhausted at condenser pressure
The expansion (or compression) of the steam is hyperbolic
All of the above
Remain same
Increases
Decreases
Behaves unpredictably
Linearly
Slowly first and then rapidly
Rapidly first and then slowly
Inversely
Provide air around burners for obtaining optimum combustion
Transport and dry the coal
Convert CO (formed in lower zone of furnace) into CO₂ at higher zone
Air delivered by induced draft fan
All the fuel burns instantaneously producing high energy release
Fuel burns with less air
Coal bursts into flame without any external ignition source but by itself due to gradual increase in temperature as a result of heat released by combination of oxygen with coal
Explosion in furnace
15 %
20 %
30 %
45 %
ηS = ηB × ηN
ηS = ηB / ηN
ηS = ηN / ηB
None of these
Evaporative capacity
Factor of evaporation
Equivalent evaporation
One boiler h.p.
Boiler efficiency, turbine efficiency, generator efficiency
All the three above plus gas cycle efficiency
Carnot cycle efficiency
Regenerative cycle efficiency
100 tonnes/h
135 tonnes/h
175 tonnes/h
250 tonnes/h
Zeroth law of thermodynamics
First law of thermodynamics
Second law of thermodynamics
None of these
Indicated power
Brake power
Efficiency
Pressure of steam
Steam evaporation rate per kg of fuel fired
Work done in evaporating 1 kg of steam per hour from and at 100°C into dry saturated steam
The evaporation of 15.65 kg of water per hour from and at 100°C into dry saturated steam
Work done by 1 kg of steam at saturation condition
48 : 20 : 15 : 7 : 10
10 : 7 : 15 : 20 : 48
20 : 48 : 7 : 15 : 10
7 : 15 : 20 : 10 : 48
I.P. = a × m + b
m = a + b × I.P.
I.P. = b × m + a
m = (b/I.P.) - a
Chimney
Centrifugal fan
Steam jet
None of these
Babcock and Wilcox
Locomotive
Lancashire
Cochran
260 kW
282 kW
296 kW
302 kW
The mechanical draught reduces the height of chimney.
The natural draught reduces the fuel consumption.
A balanced draught is a combination of induced and forced draught.
All of the above
Volume of intake steam
Pressure of intake steam
Temperature of intake steam
All of these
Blow off cock
Feed check valve
Steam stop valve
None of these
Mechanical efficiency
Overall efficiency
Indicated thermal efficiency
Brake thermal efficiency
Same as
2 times
4 times
8 times
Reheating of steam
Regenerative feed heating
Binary vapour plant
Any one of these
Horizontal
Vertical
Inclined
Both horizontal and vertical
High pressure and a low velocity
High pressure and a high velocity
Low pressure and a low velocity
Low pressure and a high velocity
Volume of intake steam
Pressure of intake steam
Temperature of intake steam
All of these