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
D. All of the above
Conduction
Convection
Radiation
None of these
Composition
Density
Porosity
All of the above
Cold body to hot body
Hot body to cold body
Smaller body to larger body
Larger body to smaller body
Q = [2πlk (T₁ - T₂)]/2.3 log (r₂/r₁)
Q = 2.3 log (r₂/r₁)/[2πlk (T₁ - T₂)]
Q = [2π (T₁ - T₂)]/2.3 lk log (r₂/r₁)
Q = = 2πlk/2.3 (T₁ - T₂) log (r₂/r₁)
Conduction
Convection
Radiation
Conduction and convection
Change vapour into liquid
Change liquid into vapour
Increase the temperature of a liquid of vapour
Convert water into steam and superheat it
Kirchoffs law
Stefan's law
Wien' law
Planck's law
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
Melting of ice
Boiler furnaces
Condensation of steam in condenser
None of these
Temperature
Wave length
Physical nature
All of the above
Improve heat transfer
Provide support for tubes
Prevent stagnation of shell side fluid
All of these
Irregular surfaces
Nonuniform temperature surfaces
One dimensional cases only
Two dimensional cases only
Equivalent thickness of film
Thermal conductivity Equivalent thickness of film Specific heat × Viscosity
Thermal conductivity Molecular diffusivity of momentum Thermal diffusivity
Film coefficient × Inside diameter Thermal conductivity
Change vapour into liquid
Change liquid into vapour
Increase the temperature of a liquid or vapour
Convert water into steam and superheat it
Radiators in automobile
Condensers and boilers in steam plants
Condensers and evaporators in refrigeration and air conditioning units
All of the above
Parallel flow
Counter flow
Cross flow
All of these
Varies with temperature
Varies with wavelength of the incident ray
Is equal to its emissivity
Does not vary with temperature and. wavelength of the incident ray
Higher
Lower
Same
Depends on the area of heat exchanger
Wien's law
Planck's law
Stefan's law
Fourier's law
Electric heater
Steam condenser
Boiler
Refrigerator condenser coils
Minimum energy
Maximum energy
Both (A) and (B)
None of these
Nature of the body
Temperature of the body
Type of surface of the body
All of these
Free electrons
Atoms colliding frequency
Low density
Porous body
More than those for liquids
Less than those for liquids
More than those for solids
Dependent on the viscosity
k/h₀
2k/h₀
h₀/k
h₀/2k
RN = hl/k
RN = μ cp/k
RN = ρ V l /μ
RN = V²/t.cp
Maximum
Minimum
Zero
None of these
Absorptive power
Emissive power
Absorptivity
Emissivity
h₁ + h₂ + h₃
(h₁.h₂.h₃)1/3
1/h₁ + 1/h₂ + 1/h₃
None of these
In conduction, reduction in the thickness of the material and an increase in thermal conductivity.
In convection, stirring of the fluid and cleaning the heating surface.
In radiation, increasing the temperature and reducing the emissivity.
All of the above