Cumulative heat drop to the isentropic heat drop
Isentropic heat drop to the heat supplied
Total useful heat drop to the total isentropic heat drop
None of the above
A. Cumulative heat drop to the isentropic heat drop
Bismuth
Copper
Aluminium
Nickel
Less efficient and less economical
Less efficient and more economical
More efficient and less economical
More efficient and more economical
There is no pressure drop due to condensation
Steam is admitted at boiler pressure and exhausted at condenser pressure
The expansion (or compression) of the steam is hyperbolic
All of the above
0.546
0.577
0.582
0.601
Coking coal
Non-coking or free burning coal
Pulverised coal
High sulphur coal
Regenerative heating
Reheating of steam
Bleeding
None of these
78-81 %
81-85 %
85-90 %
90-95 %
Horizontal
Vertical
Inclined
None of these
Same
Less
More
None of these
One-fourth
One-third
Two-fifth
One-half
Indicated power
Brake power
Efficiency
Pressure of steam
Internally fired
Externally fired
Internally as well as externally fired
None of these
Vb = 0.5 V cosα
Vb = V cos α
Vb = 0.5 V² cosα
Vb = V² cosα
Economiser
Fusible plug
Superheater
Stop valve
Straight
Circular
Curved
None of these
Prevent flat surfaces under pressure from tearing apart
Take care of failure in shear
Take care of failure in compression
Provide support for boiler
Stationary fire tube boiler
Internally fired boiler
Horizontal boiler
All of these
Mechanical efficiency
Overall efficiency
Indicated thermal efficiency
Brake thermal efficiency
47.5 mm, 130 mm
32.5 mm, 180 mm
65.5 mm, 210 mm
24.5 mm, 65 mm
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
21 %
23 %
30 %
40 %
Area of nozzle at throat
Initial pressure and volume of steam
Final pressure of steam leaving the nozzle
Both (A) and (B)
Equal to
Less than
More than
None of these
Increases
Decreases
Remain unaffected
First increases and then decreases
Swept volume to the volume at cut-off
Volume at cut-off to the clearance volume
Volume at cut-off to the swept volume
Clearance volume to the volume at cut-off
Increases expansion ratio of steam
Reduces back pressure of steam
Reduces temperature of exhaust steam
All of these
100 kg/cm² and 540°C
1 kg/cm² and 100°C
218 kg/cm² abs and 373°C
218 kg/cm² abs and 540°C
Equal to
Less than
Greater than
None of these
Superheat the steam
Reduce fuel consumption
Increase steam pressure
All of these
Entropy
Enthalpy
Pressure
Temperature