Lancashire boiler
Babcock and Wilcox boiler
Locomotive boiler
Cochran boiler
B. Babcock and Wilcox boiler
One-fourth
One-third
Two-fifth
Three-fifth
Only moving blades
Only fixed blades
Identical fixed and moving blades
Fixed and moving blades of different shape
Condenser efficiency
Vacuum efficiency
Nozzle efficiency
Boiler efficiency
Volume of intake steam
Pressure of intake steam
Temperature of intake steam
All of these
Various chemical constituents, carbon, hydrogen, oxygen etc, plus ash as percents by volume
Various chemical constituents, carbon, hydrogen, oxygen, etc, plus ash as percents by weight
Fuel constituents as percents by volume of moisture, volatile, fixed carbon and ash
Fuel constituents as percents by weight of moisture, volatile, fixed carbon and ash
There is a pressure drop in the nozzle
Fluid flows through the nozzle
Pressure drops and fluid flows through the nozzle
There is no pressure drop and fluid does not flow through the nozzle
Receiver type compound engine
Tandem type compound engine
Woolf type compound engine
None of these
30 MW
60 MW
100 MW
500 MW
Ratio of heat actually used in producing steam to the heat liberated in the furnace
Ratio of the mass of steam produced to the mass of total water supplied in a given time
Ratio of the heat liberated in the furnace to the heat actually used in producing steam
None of the above
Steam jet
Centrifugal fan
Chimney
Both (A) and (B)
40 %
25 %
50 %
80 %
Frictional losses
It is not possible to achieve 0°K temperature
Leakage
Non availability of ideal substance
Piston diameter, length of stroke and calorific value of fuel
Piston diameter, specific fuel consumption and Calorific value of fuel
Piston diameter, length of stroke and speed of rotation
Specific fuel consumption, speed of rotation and torque
Correct fuel air ratio
Proper ignition temperature
O₂ to support combustion
All the three above
Longitudinally
Circumferentially
On dished end
Anywhere
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
Coking coal
Non-coking or free burning coal
Pulverised coal
High sulphur coal
Increases
Decreases
Remain unaffected
First increases and then decreases
Receiver type
Tandem type
Woolf type
All of these
40 %
50 %
75 %
90 %
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
Linearly
Slowly first and then rapidly
Rapidly first and then slowly
Inversely
Equal
Half
Double
Four times
Mechanical fan
Chimney
A steam jet
All of these
Form lumps or masses of coke
Burn freely
Show little or no fusing action
Burn completely
100°C
Above dew point temperature of flue gases
Below dew point temperature of flue gases
Less than wet bulb temperature of flue gases
To blow off steam when the pressure of steam inside the boiler exceeds the working pressure
To indicate the water level inside the boiler to an observer
To measure pressure of steam inside the steam boiler
None of the above
Mean diameter and thickness
Inside diameter and thickness
Outside diameter and thickness
Outside diameter and inside diameter
1 m
2 m
3 m
4 m
Control the flow of steam from the boiler to the main pipe and to shut off the steam completely when required
Empty the boiler when required and to discharge the mud, scale or sediments which are accumulated at the bottom of the boiler
Put off fire in the furnace of the boiler when the level of water in the boiler falls to an unsafe limit
Increase the temperature of saturated steam without raising its pressure