Heat carried away by flue gases
Heat carried away by ash
Moisture present in fuel and steam formed by combustion of hydrogen in fuel
All of the above
D. All of the above
Constant volume
Constant temperature
Constant pressure
Constant entropy
Large marine propulsion
Electric power generation
Direct drive of fans, compressors, pumps
All of these
The steam is allowed to expand in the nozzle, where it gives a high velocity before it enters the moving blades
The expansion of steam takes place partly in the fixed blades and partly in the moving blades
The steam is expanded from a high pressure to a condenser pressure in one or more nozzles
The pressure and temperature of steam remains constant
To provide reciprocating motion to the slide valve
To convert reciprocating motion of the piston into rotary motion of the crank
To convert rotary motion of the crankshaft into to and fro motion of the valve rod
To provide simple harmonic motion to the D-slide valve
Give maximum space
Give maximum strength
Withstand pressure inside boiler
Resist intense heat in fire box
T1 /88.25H
88.25H/T1
T1 /176.5H
176.5H/T1
Horizontal
Vertical
Inclined
Both horizontal and vertical
3.3 bar
5.46 bar
8.2 bar
9.9 bar
1 m
2 m
3 m
4 m
Wet
Superheated
Remain dry saturated
Dry
Heating the oil in the settling tanks
Cooling the oil in the settling tanks
Burning the oil
Suspension
It increases the thermodynamic efficiency of the turbine
Boiler is supplied with hot water
It decreases the power developed by the turbine
All of the above
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
LaMont boiler
Lancashire boiler
Velox boiler
Benson boiler
Degree of super-saturation
Degree of superheat
Degree of under-cooling
None of these
50°C and normal atmospheric pressure
50°C and 1.1 bar pressure
100°C and normal atmospheric pressure
100°C and 1.1 bar pressure
Moisture in fuel
Dry flue gases
Steam formation
Unburnt carbon
Decrease dryness fraction of steam
Decrease specific volume of steam
Increase the entropy
Increase the heat drop
Unburnt carbon in ash
Incomplete combustion
Ash content
Flue gases
Centrifugal pump
Axial flow pump
Gear pump
Reciprocating pump
Steam enters and exhausts through the same port
Steam enters at one end and exhausts at the centre
Steam enters at the centre and exhausts at the other end
None of the above
DIN
BS
ASTM
IBR
539 kcal/ kg
539 BTU/ lb
427 kcal/ kg
100 kcal/ kg
Indicated power
Brake power
Frictional power
None of these
Higher calorific value at constant volume
Lower calorific value at constant volume
Higher calorific value at constant pressure
Lower calorific value at constant pressure
The power required and working pressure
The geographical position of the power house
The fuel and water available
All of the above
More
Less
Equal
None of these
Fixed blades
Moving blades
Both fixed and moving blades
None of these
180° to each other
90° to each other
0° to each other
None of these
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