The better insulation must be put inside
The better insulation must be put outside
One could place either insulation on either side
One should take into account the steam temperature before deciding as to which insulation is put where
A. The better insulation must be put inside
Change vapour into liquid
Change liquid into vapour
Increase the temperature of a liquid or vapour
Convert water into steam and superheat it
It is impossible to transfer heat from low temperature source to t high temperature source
Heat transfer by radiation requires no medium
All bodies above absolute zero emit radiation
Heat transfer in most of the cases takes place by combination of conduction, convection and radiation
Q = 2πkr1 r2 (T1 - T2)/ (r2 - r1)
Q = 4πkr1 r2 (T1 - T2)/ (r2 - r1)
Q = 6πkr1 r2 (T1 - T2)/ (r2 - r1)
Q = 8πkr1 r2 (T1 - T2)/ (r2 - r1)
Zeroth law of thermodynamics
First law of thermodynamics
Second law of thermodynamics
Kirchhoff's law
Grashoff number
Biot number
Stanton number
Prandtl number
Nature of the body
Temperature of the body
Type of surface of the body
All of these
Directly proportional to the thermal conductivity
Inversely proportional to density of substance
Inversely proportional to specific heat
All of the above
Directly proportional to the surface area of the body
Directly proportional to the temperature difference on the two faces of the body
Dependent upon the material of the body
All of the above
Its temperature
Nature of the body
Kind and extent of its surface
All of the above
Thermal conductivity to the equivalent thickness of the film of fluid
Temperature drop through the films of fluids to the thickness of film of fluids
Thickness of film of fluid to the thermal conductivity
Thickness of film of fluid to the temperature drop through the films of fluids
Below which a gas does not obey gas laws
Above which a gas may explode
Below which a gas is always liquefied
Above which a gas will never liquefied
Cold water inlet and outlet
Hot medium inlet and outlet
Hot medium outlet and cold water inlet
Hot medium outlet and cold water outlet
Same
Higher
More or less same
Very much lower
P = 0, x = 0 and a = 1
P=1, x = 0, and a = 0
P = 0, T= 1, and a = 0
X = 0, a + p = 1
Radiators in automobile
Condensers and boilers in steam plants
Condensers and evaporators in refrigeration and air conditioning units
All of the above
High thickness of insulation
High vapour pressure
Less thermal conductivity insulator
A vapour seal
1 : 1
2 : 1
1 : 2
4 : 1
Parallel flow type
Counter flow type
Cross flow type
Regenerator type
Directly proportional to thermal conductivity
Inversely proportional to density of substance
Inversely proportional to specific heat
All of the above
Velocity reduction method
Equal friction method
Static regains method
Dual or double method
k/h₀
2k/h₀
h₀/k
h₀/2k
P = 0, x = 0 and a = 1
P=1, T = 0 and a = 0
P = 0, x = 1 and a = 0
X = 0, a + p = 1 Where a = absorptivity, p = reflectivity, x = transmissivity
Increases
Decreases
Remain constant
May increase or decrease depending on temperature
Irregular surfaces
Nonuniform temperature surfaces
One dimensional cases only
Two dimensional cases only
Wien's law
Stefan's law
Kirchhoff's law
Planck's law
Aluminium
Steel
Brass
Copper
h = k/ ρS
h = ρS/k
h = S/ρk
h = kρ/S
Grashoff number
Nusselt number
Weber number
Prandtl number
Solids
Liquids
Gases
None of these
Blast furnace
Heating of building
Cooling of parts in furnace
Heat received by a person from fireplace