Safety valve
Water level indicator
Pressure gauge
Fusible plug
A. Safety valve
0.4
0.56
0.67
1.67
Vb = 0.5 V cosα
Vb = V cos α
Vb = 0.5 V² cosα
Vb = V² cosα
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
Velocity compounding
Pressure compounding
Pressure-velocity compounding
All of these
Enthalpy
Superheating
Super saturation
Latent heat
No heat drop in moving blades
No heat drop in fixed blades
Maximum heat drop in moving blades
Maximum heat drop in fixed blades
Same value
Higher value
Lower value
Lower/higher depending on steam flow
Mean diameter and thickness
Inside diameter and thickness
Outside diameter and thickness
Outside diameter and inside diameter
Serve as storage of steam
Serve as storage of feed water for water wall
Remove salts from water
Separate steam from water
Choked
Under-damping
Over-damping
None of these
Economiser
Fusible plug
Superheater
Stop valve
Single rotor impulse turbine
Multi-rotor impulse turbine
Impulse reaction turbine
None of these
Cylinder feed indicated mass of steam
Cylinder feed + indicated mass of steam
Mass of cushion steam + indicated mass of steam
Mass of cushion steam + cylinder feed
0.546
0.577
0.582
0.601
Wet steam
Dry saturated steam
Superheated steam
None of these
1.5 m, 4 m
1.5 m, 6 m
1 m, 4 m
2 m, 4 m
Ratio of heat actually used in producing steam to the heat liberated in the furnace
Ratio of the mass of steam produced to the mass of total water supplied in a given time
Ratio of the heat liberated in the furnace to the heat actually used in producing steam
None of the above
Reheating of steam
Regenerative feed heating
Binary vapour plant
Any one of these
Degree of super-saturation
Degree of superheat
Degree of under-cooling
None of these
Vb = 0.5 V cosα
Vb = V cosα
Vb = 0.5 V² cosα
Vb = V² cosα
1 to 2 m
1.25 to 2.25 m
1.5 to 2.5 m
1.75 to 2.75 m
The draft to be created
Limitation of construction facilities
Control of pollution
Quantity of flue gases to be handled
Only moving blades
Only fixed blades
Identical fixed and moving blades
Fixed and moving blades of different shape
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
1.02 to 1.06
1.08 to 1.10
1.2 to 1.6
1.6 to 2
Same
Less
More
None of these
Cornish is fire tube and Lancashire is water tube
Cornish is water tube and Lancashire is fire tube
Cornish has two fire tubes and Lancashire has one
Lancashire has two fire tubes and Cornish has one
Longitudinally
Circumferentially
On dished end
Anywhere
Simple reaction turbine
Velocity compounded turbine
Pressure compounded turbine
Pressure-velocity compounded turbine
Increases
Decreases
Remain unaffected
First increases and then decreases