1.5 to 2 m
2.5 to 3.5 m
3.5 to 4.5 m
None of these
B. 2.5 to 3.5 m
Water space also
Chimney
Steam space
Superheater
Same
More
Less
Less or more depending on size of boiler
21 %
23 %
30 %
40 %
100 bar
150 bar
200 bar
250 bar
Pulverising coal in inert atmosphere
Heating wood in a limited supply of air at temperatures below 300°C
Strongly heating coal continuously for about 48 hours in the absence of air in a closed vessel
Binding the pulverised coal into briquettes
Non-coking bituminous coal
Brown coal
Pulverised coal
Coking bituminous coal
Equals that of the surroundings
Equals 760 mm of mercury
Equals to atmospheric pressure
Equals the pressure of water in the container
Regeneration
Reheating of steam
Both (A) and (B)
Cooling of steam
Remains constant
Increases
Decreases
Behaves unpredictably
Lowers the boiling point of a liquid
Raises the boiling point of a liquid
Does not affects the boiling point of a liquid
Reduces its volume
Divergent nozzle
Convergent nozzle
Convergent-divergent nozzle
None of these
Horizontal multi-tubular water tube boiler
Water wall enclosed furnace type
Vertical tubular fire tube type
Horizontal multi-tubular fire tube type
180° to each other
90° to each other
0° to each other
None of these
Avoid excessive build up of pressure
Avoid explosion
Extinguish fire if water level in the boiler falls below alarming limit
Control steam dome
Velocity increases
Velocity decreases
Velocity remains constant
Pressure remains constant
1 to 1.25m
1 to 1.75 m
2 to 4 m
1.75 to 2.75 m.
ηS = ηB × ηN
ηS = ηB / ηN
ηS = ηN / ηB
None of these
The draft to be created
Limitation of construction facilities
Control of pollution
Quantity of flue gases to be handled
Linearly
Slowly first and then rapidly
Rapidly first and then slowly
Inversely
Volume
Pressure
Entropy
Enthalpy
Locomotive boiler
Cochran boiler
Cornish boiler
Babcock and Wilcox boiler
Direction of steam flow
Number of stages
Mode of steam action
All of these
No heat drop in moving blades
No heat drop in fixed blades
Maximum heat drop in moving blades
Maximum heat drop in fixed blades
47.5 mm, 130 mm
32.5 mm, 180 mm
65.5 mm, 210 mm
24.5 mm, 65 mm
24 m
35 m
57.5 m
79 m
From a metal wall from one medium to another
From heating an intermediate material and then heating the air from this material
By direct mixing,
Heat is transferred by bleeding some gases from furnace
Decrease the mass flow rate and to increase the wetness of steam
Increase the mass flow rate and to increase the exit temperature
Decrease the mass flow rate and to decrease the wetness of steam
Increase the exit temperature without any effect on mass flow rate
Horizontal
Vertical
Inclined
Both horizontal and vertical
40 %
25 %
50 %
80 %
Moisture in fuel
Dry flue gases
Steam formation
Unburnt carbon