Multi tubular
Horizontal
Internally fired
All of the above
D. All of the above
Indicated power
Brake power
Efficiency
Pressure of steam
Same
Less
More
None of these
Keep the burner tips cool
Aid in proper combustion
Because sputtering, possibly extinguishing flame
Clean the nozzles
Blow off cock
Feed check valve
Steam stop valve
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
High calorific value
Produce minimum smoke and gases
Ease in storing
High ignition point
Lever safety valve
Dead weight safety valve
High steam and low water safety valve
Spring loaded safety valve
Increases
Decreases
Remain same
None of these
2 cm
6 cm
8 cm
12 cm
78-81 %
81-85 %
85-90 %
90-95 %
From a metal wall from one medium to another
From heating an intermediate material and then heating the air from this material
By direct mixing
Heat is transferred by bleeding some gas from furnace
Horizontal
Vertical
Inclined
Horizontal and inclined
More
Less
Equal
None of these
Piston diameter, length of stroke and calorific value of fuel
Piston diameter, specific fuel consumption and Calorific value of fuel
Piston diameter, length of stroke and speed of rotation
Specific fuel consumption, speed of rotation and torque
Desirable
Economical
Essential
Uneconomical
Superheater
Air-preheater
Economiser
Injector
To reduce the ratio of expansion in each cylinder
To reduce the length of stroke
To reduce the temperature range in each cylinder
All of the above
Approach temperature should be as low as possible
Handling and maintenance should be easier
Heat transfer area should be optimum
Stack gases should not be cooled to the dew point
0.007 bar
0.053 bar
0.06 bar
0.067 bar
The power required and working pressure
The geographical position of the power house
The fuel and water available
All of the above
CO₂
CO
O₂
N₂
Direction of steam flow
Number of stages
Mode of steam action
All of these
p₁. p₂
p₁/p₂
p₂/p₁
p₁ + p₂
Blow off cock
Fusible plug
Superheater
Stop valve
Cavitation of boiler feed pumps
Corrosion caused by oxygen
Heat transfer coefficient
pH value of water
Drooping characteristic
Linear characteristic
Rising characteristic
Flat characteristic
Reheating of steam
Regenerative feed heating
Binary vapour plant
Any one of these
Swept volume to the volume at cut-off
Clearance volume to the swept volume
Volume at cut-off to the swept volume
Swept volume to the clearance volume
Wet steam
Dry saturated steam
Superheated steam
None of these
Steam evaporation rate per kg of fuel fired
Work done in evaporating 1 kg of steam per hour from and at 100°C into dry saturated steam
The evaporation of 15.65 kg of water per hour from and at 100°C into dry saturated steam
Work done by 1 kg of steam at saturation condition