Horizontal fire tube boiler
Horizontal water tube boiler
Vertical water tube boiler
Vertical fire tube boiler
D. Vertical fire tube boiler
Climatic conditions
Temperature of furnace gases
Height of chimney
All of these
Infinitely long
Around 200 meters
Equal to the height of the hot gas column producing draught
Outside temperature is very low
1.5 to 2 m
2.5 to 3.5 m
3.5 to 4.5 m
None of these
1000 J
360 kJ
3600 kJ
3600 kW/sec
Workdone on the blades to the energy supplied to the blades
Workdone on the blades per kg of steam to the total energy supplied per stage per kg of steam
Energy supplied to the blades per kg of steam to the total energy supplied per stage per kg of steam
None of the above
More
Less
Same
None of these
0.546
0.577
0.582
0.601
Steam pressure exceeds the working pressure
Water level in the boiler becomes too low
Both (A) and (B)
None of the above
Better burning
More calorific value
Less radiation loss
Medium sized units
1 kg/cm²
5 kg/cm²
10 kg/cm²
18 kg/cm²
Increased work output per unit mass of steam
Decreased work output per unit mass of steam
Increased thermal efficiency
Decreased work output per unit mass of steam as well as increased thermal efficiency
(p₂/p₁) = [2/(n - 1)] n/(n + 1)
(p₂/p₁) = [2/(n + 1)] n/(n-1)
(p₂/p₁) = [(n - 1)/2] n + (1/n)
(p₂/p₁) = [(n + 1)/2] n - (1/n)
100 tonnes/h
135 tonnes/h
175 tonnes/h
250 tonnes/h
Corrosion
Scale
Carryover
All of the above
Equal to
Less than
More than
None of these
(h - hf1)/2257
(h + hf1)/2257
(h × hf1)/2257
None of these
Increases
Decreases
Remain constant
May increase or decrease depending upon the method of storage
Equal to
Lower than
Higher than
None of these
Carbon, hydrogen, nitrogen, sulphur, moisture
Fixed carbon, ash, volatile matter, moisture
Higher calorific value
Lower calorific value
Divergent nozzle
Convergent nozzle
Convergent-divergent nozzle
None of these
One-fourth
One-third
Two-fifth
Three-fifth
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
Lever safety valve
Dead weight safety valve
High steam and low water safety valve
Spring loaded safety valve
Heated sufficiently
Burnt in excess air
Heated to its ignition point
Burnt as powder
Vertical fire tube type
Horizontal fire tube type
Horizontal water tube type
Forced circulation type
Surface condenser
Jet condenser
Barometric condenser
Evaporative condenser
Enthalpy
Superheating
Super saturation
Latent heat
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
Horizontal straight line
Vertical straight line
Straight inclined line
Curved line
Horizontal
Vertical
Inclined
None of these