Induced draft fan and chimney
Induced draft fan and forced draft fan
Forced draft fan and chimney
Any one of the above
B. Induced draft fan and forced draft fan
Low
Very low
High
Very high
0.17 MN/m²
1.7 MN/m²
17 MN/m²
170 MN/m²
Heat transfer takes place across cylinder walls
Work is done
Steam may be wet, dry or superheated after expansion
All of the above
Equal
Less
More
None of these
Corrosion
Scale
Carryover
All of the above
47.5 mm, 130 mm
32.5 mm, 180 mm
65.5 mm, 210 mm
24.5 mm, 65 mm
The efficient steam jacketing of the cylinder walls
Superheating the steam supplied to the engine cylinder
Keeping the expansion ratio small in each cylinder
All of the above
Heat transfer takes place
Work is done by the expanding steam
Internal energy of steam changes
None of the above
Receiver type
Tandem type
Woolf type
All of these
6.25 mm
62.5 mm
72.5 mm
92.5 mm
Serve as storage of steam
Serve as storage of feed water for water wall
Remove salts from water
Separate steam from water
Boiler efficiency, turbine efficiency, generator efficiency
All the three above plus gas cycle efficiency
Carnot cycle efficiency
Regenerative cycle efficiency
24 m
35 m
57.5 m
79 m
75
115
165
225
Constant volume
Constant temperature
Constant pressure
Constant entropy
Blading efficiency
Nozzle efficiency
Stage efficiency
Mechanical efficiency
Provide air around burners for obtaining optimum combustion
Transport and dry the coal
Cool the scanners
Convert CO (formed in lower zone of furnace) into CO₂ at higher zone.
The ratio of heat actually used in producing the steam to the heat liberated in the furnace
The amount of water evaporated or steam produced in kg per kg of fuel burnt
The amount of water evaporated from and at 100° C into dry and saturated steam
The evaporation of 15.653 kg of water per hour from and at 100° C
And its corresponding conversion into dry saturated steam at 100°C and 1.033 kg/cm²
And its corresponding conversion into dry steam at desired boiler pressure
Conversion into steam at atmospheric condition
Conversion into steam at the same pressure at which feed water is supplied
Frictional losses
It is not possible to achieve 0°K temperature
Leakage
Non availability of ideal substance
Water passes through the tubes which are surrounded by flames and hot gases
The flames and hot gases pass through the tubes which are surrounded by water
Forced circulation takes place
None of these
200-400 kcal/ kg
800-1200 kcal/ kg
2000-4000 kcal/ kg
5000-8000 kcal/ kg
Initial pressure and superheat
Exit pressure
Turbine stage efficiency
All of these
Amount of water evaporated per hour
Steam produced in kg/h
Steam produced in kg/kg of fuel burnt
All of these
Drooping characteristic
Linear characteristic
Rising characteristic
Flat characteristic
Absolute velocity at the inlet of moving blade is equal to that at the outlet
Relative velocity at the inlet of the moving blade is equal to that at the outlet
Axial velocity at inlet is equal to that at the outlet
Whirl velocity at inlet is equal to that at the outlet
Lancashire boiler
Babcock and Wilcox boiler
Locomotive boiler
Cochran boiler
Bleeding
Reheating
Governing
None of these
0.5 to 10 MN/m²
1 to 15 MN/m²
2.5 to 15 MN/m²
3.5 to 20 MN/m²
When the cross-section of the nozzle increases continuously from entrance to exit
When the cross-section of the nozzle decreases continuously from entrance to exit
When the cross-section of the nozzle first decreases from entrance to throat and then increases from its throat to exit
None of the above