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
D. All of the above
No heat drop in moving blades
No heat drop in fixed blades
Maximum heat drop in moving blades
Maximum heat drop in fixed blades
p₁. p₂
p₁/p₂
p₂/p₁
p₁ + p₂
Number of casing
Number of entries of steam
Number of exits of steam
Each row of blades
Serve as storage of steam
Serve as storage of feed water for water wall
Remove salts from water
Separate steam from water
Blow off cock
Feed check valve
Economiser
Fusible plug
Increases
Decreases
Remain constant
May increase or decrease depending upon the method of storage
Maintain the speed of the turbine
Reduce the effective heat drop
Reheat the steam and improve its quality
Completely balance against end thrust
Temperature, time, and turbulence
Total air, true fuel, and turbulence
Thorough mixing, total air and temperature
Total air, time, and temperature
60°
90°
180°
270°
Diagram efficiency
Nozzle efficiency
Gross efficiency
None of these
Zero
Minimum
Maximum
None of these
Piston rod
Connecting rod
Eccentric rod
Valve rod
0.546
0.577
0.582
0.601
Volume
Pressure
Entropy
Enthalpy
Non-coking bituminous coal
Brown coal
Peat
None of the above
Provide air around burners for obtaining optimum combustion
Transport and dry the coal
Convert CO (formed in lower zone of furnace) into CO₂ at higher zone
Air delivered by induced draft fan
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
Supply of excess, air
Supply of excess coal
Burning CO and unburnts in upper zone of furnace by supplying more air
Fuel bed firing
Large marine propulsion
Electric power generation
Direct drive of fans, compressors, pumps
All of these
I.P. = a × m + b
m = a + b × I.P.
I.P. = b × m + a
m = (b/I.P.) - a
Condenser efficiency
Nozzle efficiency
Boiler efficiency
Vacuum efficiency
Induced steam jet draught
Chimney draught
Forced steam jet draught
None of these
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
Receiver type compound engine
Tandem type compound engine
Woolf type compound engine
Both (A) and (B)
Water
Dry steam
Wet steam
Super heated steam
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
Corrosion
Scale
Carryover
All of the above
Mechanical efficiency
Overall efficiency
Indicated thermal efficiency
Brake thermal efficiency
Increases
Decreases
Remains unchanged
Increases/decreases depending on steam temperature requirements
Essentially an isentropic process
Non-heat transfer process
Reversible process
Constant temperature process