Same value
Higher value
Lower value
Lower/higher depending on steam flow
B. Higher value
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
Anthracite coal
Bituminous coal
Lignite
Peat
Infinitely long
Around 200 meters
Equal to the height of the hot gas column producing draught
Outside temperature is very low
As an impulsive force
As a reaction force
Partly as an impulsive force and partly as a reaction force
None of the above
Locomotive boiler
Cochran boiler
Cornish boiler
Babcock and Wilcox boiler
Barometric pressure + actual pressure
Barometric pressure - actual pressure
Gauge pressure + atmospheric pressure
Gauge pressure - atmospheric pressure
Flue gases pass through tubes and water around it
Water passes through the tubes and flue gases around it
Forced circulation takes place
Tubes are laid vertically
1.5 to 2 m
2.5 to 3.5 m
3.5 to 4.5 m
None of these
Remain same
Increases
Decreases
Behaves unpredictably
Initial conditions of steam
Back pressure
Initial pressure of steam
All of these
0.007 bar
0.053 bar
0.06 bar
0.067 bar
Non-coking bituminous coal
Brown coal
Pulverised coal
Coking bituminous coal
Induced draft fan
Smoke meter
Chimney
Precipitator
Solid and vapour phases are in equilibrium
Solid and liquid phases are in equilibrium
Liquid and vapour phases are in equilibrium
Solid, liquid and vapour phases are in equilibrium
Heating takes place at bottom and the water supplied at bottom gets converted into the mixture of steam bubbles and hot water which rise to drum
Water is supplied in drum and through down comers located in atmospheric condition it passes to the water wall and rises to drum in the form of mixture of water and steam
Feed pump is employed to supplement natural circulation in water wall type furnace
Water is converted into steam in one pass without any recirculation
539 kcal/ kg
539 BTU/ lb
427 kcal/ kg
100 kcal/ kg
260 kW
282 kW
296 kW
302 kW
More
Equal
Less
Could be more or less depending on the size of plant
Prevent the bulging of flat surfaces
Avoid explosion in furnace
Prevent leakage of hot flue gases
Support furnace freely from top
1 kg
4/3 kg
8/3 kg
2 kg
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
Pressure only
Temperature only
Dryness fraction only
Pressure and dryness fraction
Same value
Higher value
Lower value
Lower/higher depending on steam flow
Steam temperature remains constant
Steam pressure remains constant
Steam enthalpy remains constant
Steam entropy remains constant
1 kg/cm
6 kg/cm
17 kg/cm²
100 kg/cm²
Increase thermal efficiency of boiler
Economise on fuel
Extract heat from the exhaust flue gases
Increase flue gas temperature
1.5 m, 4 m
1.5 m, 6 m
1 m, 4 m
2 m, 4 m
Stationary < fire tube type
Horizontal type
Natural circulation type
All of the above
Ash
Volatile matter
Moisture
Hydrogen
0.1 to 0.2 kg
0.2 to 0.4 kg
0.6 to 0.8 kg
1.0 to 1.5 kg