Boyle's law
Charles' law
Gay-Lussac law
Avogadro's law
A. Boyle's law
12
14
16
32
In the middle
At the tip below the load
At the support
Anywhere
The liquid fuels have higher calorific value than solid fuels
The solid fuels have higher calorific value than liquid fuels
A good fuel should have low ignition point
The liquid fuels consist of hydrocarbons
Th > Ts
Th < Ts
Th = Ts
None of these
Same
Double
Half
Four times
11/7
9/7
4/7
All of the above
Same
Half
Two times
Four times
No stress
Shear stress
Tensile stress
Compressive stress
t
2t
4t
8t
Butt joint
Lap joint
Double riveted lap joints
All types of joints
No stress
Shear stress
Tensile stress
Compressive stress
Pulverised coal
Brown coal
Coking bituminous coal
Non-coking bituminous coal
(σx/2) + (1/2) × √(σx² + 4 τ²xy)
(σx/2) - (1/2) × √(σx² + 4 τ²xy)
(σx/2) + (1/2) × √(σx² - 4 τ²xy)
(1/2) × √(σx² + 4 τ²xy)
External energy
Internal energy
Kinetic energy
Molecular energy
One
Two
Three
Four
Carnot cycle
Bell-Coleman cycle
Rankine cycle
Stirling cycle
10 MPa
30 MPa
50 MPa
100 MPa
It is possible to transfer heat from a body at a lower temperature to a body at a higher temperature.
It is impossible to transfer heat from a body at a lower temperature to a body at a higher temperature, without the aid of an external source.
It is possible to transfer heat from a body at a lower temperature to a body at a higher temperature by using refrigeration cycle.
None of the above
Carnot cycle
Rankine cycle
Brayton cycle
Bell Coleman cycle
Maximum shear stress
No shear stress
Minimum shear stress
None of the above
Two constant pressure
Two constant volume
Two isentropic
One constant pressure, one constant volume
Two constant volume and two isentropic processes
Two isothermal and two isentropic processes
Two constant pressure and two isentropic processes
One constant volume, one constant pressure and two isentropic processes
Rankine
Stirling
Carnot
Brayton
Increase
Decrease
Remain unchanged
Increase/decrease depending on application
Brayton cycle
Joule cycle
Carnot cycle
Reversed Brayton cycle
√(KT/m)
√(2KT/m)
√(3KT/m)
√(5KT/m)
v1/v2
v2/v1
(v1 + v2)/v1
(v1 + v2)/v2
65° to 220°C
220° to 345°C
345° to 470°C
470° to 550°C
Thermal efficiency
Work ratio
Avoids pollution
None of these
Zero
Minimum
Maximum
Infinity