Minimum
Maximum
Zero
None of these
C. Zero
When the cross-section of the nozzle increases continuously from entrance to exit
When the cross-section of the nozzle decreases continuously from entrance to exit
When the cross-section of the nozzle first decreases from entrance to throat and then increases from its throat to exit
None of the above
Pulverising coal in inert atmosphere
Heating wood in a limited supply of air at temperatures below 300°C
Strongly heating coal continuously for about 48 hours in the absence of air in a closed vessel
Binding the pulverised coal into briquettes
To provide an adequate supply of air for the fuel combustion
To exhaust the gases of combustion from the combustion chamber
To discharge the gases of combustion to the atmosphere through the chimney
All of the above
Pressure increases while velocity decreases
Pressure decreases while velocity increases
Pressure and velocity both decreases
Pressure and velocity both increases
(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)
Internally fired boiler
Externally fired boiler
Natural circulation boiler
Forced circulation boiler
Blading efficiency
Nozzle efficiency
Gross or stage efficiency
Mechanical efficiency
Babcock and Wilcox
Locomotive
Lancashire
Cochran
0.17 MN/m²
1.7 MN/m²
17 MN/m²
170 MN/m²
Receiver type
Tandem type
Woolf type
All of these
Complete account of heat supplied by 1 kg of dry fuel and the heat consumed
Moisture present in the fuel
Steam formed by combustion of hydrogen per kg of fuel
All of the above
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
225.65 kgf/ cm²
273 kgf/ cm²
100 kgf/ cm²
1 kgf/ cm²
Boiler effectiveness
Boiler evaporative capacity
Factor of evaporation
Boiler efficiency
Receiver type compound engine
Tandem type compound engine
Woolf type compound engine
Both (A) and (B)
0.546
0.577
0.582
0.601
Entropy
Enthalpy
Pressure
Temperature
Essentially an isentropic process
Non-heat transfer process
Reversible process
Constant temperature process
180° to each other
90° to each other
0° to each other
None of these
Equal to
Less than
Greater than
None of these
Drooping characteristic
Linear characteristic
Rising characteristic
Flat characteristic
Induced draft fan and chimney
Induced draft fan and forced draft fan
Forced draft fan and chimney
Any one of the above
Throttle governing
Cut-off governing
By-pass governing
None of these
Zero
Minimum
Maximum
None of these
Wet
Superheated
Remain dry saturated
Dry
Throttling calorimeter
Separating calorimeter
Combined separating and throttling calorimeter
Bucket calorimeter
Work done during the Rankine cycle
Work done during compression
Work done during adiabatic expansion
Change in enthalpy
12 m
1.52.5 m
23 m
2.53.5 m
Steam boiler
Steam turbine
Steam condenser
Steam injector
Slow speed engine
Medium speed steam engine
High speed steam engine
None of these