Stationary < fire tube type
Horizontal type
Natural circulation type
All of the above
D. All of the above
Moisture in fuel
Dry flue gases
Steam formation
Unburnt carbon
Centrifugal pump
Axial flow pump
Gear pump
Reciprocating pump
Former is fire tube type and latter is water tube type boiler
Former is water tube type and latter is fire tube type
Former contains one fire tube and latter contains two fire tubes
None/of the above
Absolute velocity at the inlet of moving blade is equal to that at the outlet
Relative velocity at the inlet of the moving blade is equal to that at the outlet
Axial velocity at inlet is equal to that at the outlet
Whirl velocity at inlet is equal to that at the outlet
Vb = 0.5 V cosα
Vb = V cos α
Vb = 0.5 V² cosα
Vb = V² cosα
Minimum
Maximum
Zero
None of these
56 %
63 %
74 %
78 %
To determine the generating capacity of the boiler
To determine the thermal efficiency of the boiler when working at a definite pressure
To prepare heat balance sheet for the boiler
All of the above
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
Blades are equiangular
Blade velocity coefficient is unity
Blades are equiangular and frictionless
Blade solidity is 0.65
1 kg/cm
6 kg/cm
17 kg/cm²
100 kg/cm²
V = 44.72 hd K
V = 44.72 K hd
V = 44.72 K hd
V = 44.72 K hd
24 m
35 m
57.5 m
79 m
Pressure increases while velocity decreases
Pressure decreases while velocity increases
Pressure and velocity both decreases
Pressure and velocity both increases
Same
More
Less
Less or more depending on size of boiler
Horizontal
Vertical
Inclined
None of these
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
Choked
Under-damping
Over-damping
None of these
5 to 6 m
6 to 7 m
7.25 to 9 m
9 to 10 m
Regenerative heating
Reheating of steam
Bleeding
None of these
Has high heating value
Retards electric precipitation
Promotes complete combustion
Has highly corrosive effect
Mean diameter and thickness
Inside diameter and thickness
Outside diameter and thickness
Outside diameter and inside diameter
421 kg.m
421 kg.m
539 kg.m
102 kg.m
Initial conditions of steam
Back pressure
Initial pressure of steam
All of these
Increases
Decreases
Remains constant
None of these
Equals that of the surroundings
Equals 760 mm of mercury
Equals to atmospheric pressure
Equals the pressure of water in the container
I.P. = a × m + b
m = a + b × I.P.
I.P. = b × m + a
m = (b/I.P.) - a
Lowest temperature at which oil will flow under set condition
Storage temperature
Temperature at which fuel is pumped through burners
Temperature at which oil is transported
Drooping characteristic
Linear characteristic
Rising characteristic
Flat characteristic
Amount of water evaporated per hour
Steam produced in kg/h
Steam produced in kg/kg of fuel burnt
All of these