Approach temperature should be as low as possible
Handling and maintenance should be easier
Heat transfer area should be optimum
Stack gases should not be cooled to the dew point
D. Stack gases should not be cooled to the dew point
At the entrance to the nozzle
At the throat of the nozzle
In the convergent portion of the nozzle
In the divergent portion of the nozzle
Equivalent evaporation
Factor of evaporation
Boiler efficiency
Power of a boiler
Boil
Flash i.e. get converted into steam
Remain as it was
Cool down
Swept volume to the volume at cut-off
Clearance volume to the swept volume
Volume at cut-off to the swept volume
Swept volume to the clearance volume
Constant volume
Constant temperature
Constant pressure
Constant entropy
Mechanical efficiency
Overall efficiency
Indicated thermal efficiency
Brake thermal efficiency
Mechanical efficiency
Overall efficiency
Indicated thermal efficiency
Brake thermal efficiency
Barometric pressure + actual pressure
Barometric pressure - actual pressure
Gauge pressure + atmospheric pressure
Gauge pressure - atmospheric pressure
To dry flue gases
In moisture present in the fuel
To steam formed by combustion of hydrogen per kg of fuel
All of the above
3.3 bar
5.46 bar
8.2 bar
9.9 bar
Stage efficiency
Internal efficiency
Rankine efficiency
None of these
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
Internally fired boiler
Externally fired boiler
Natural circulation boiler
Forced circulation boiler
100°C
Above dew point temperature of flue gases
Below dew point temperature of flue gases
Less than wet bulb temperature of flue gases
Heat drop in fixed blades to the heat drop in moving blades
Heat drop in moving blades to the heat drop in fixed blades
Heat drop in moving blades to the heat drop in fixed blades plus heat drop in moving blades
Heat drop in fixed blades plus heat drop in moving blades to the heat drop in moving blades
Mechanical fan
Chimney
A steam jet
All of these
1 to 2 m
1.25 to 2.25 m
1.5 to 2.5 m
1.75 to 2.75 m
To draw water
To circulate water
To drain off the water
All of these
Non-coking bituminous coal
Brown coal
Peat
None of the above
Wet steam
Saturated steam
Superheated steam
Cushion steam
Centrifugal pump
Axial flow pump
Gear pump
Reciprocating pump
Surface condenser
Jet condenser
Barometric condenser
Evaporative condenser
Induced draft fan and chimney
Induced draft fan and forced draft fan
Forced draft fan and chimney
Any one of the above
Air present in atmosphere at NTP conditions
Air required for complete combustion of fuel with no excess air
Air required for optimum combustion so as to have reasonable excess air
Air required to convert CO into CO₂
Indicated power
Brake power
Frictional power
None of these
Horizontal
Vertical
Inclined
None of these
100 tonnes/h
135 tonnes/h
175 tonnes/h
250 tonnes/h
Fixed blades
Moving blades
Both fixed and moving blades
None of these
Decreasing initial steam pressure and temperature
Increasing exhaust pressure
Decreasing exhausts pressure
Increasing the expansion ratio
Increases
Decreases
Remain constant
May increase or decrease depending upon the method of storage