Temperature
Thickness
Area
Time
D. Time
Reynold's number
Grashoff's number
Reynold's number, Grashoff's number
Prandtl number, Grashoff's number
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
Conduction
Convection
Radiation
None of these
Conduction
Convection
Radiation
None of these
The total radiation from a black body per second per unit area is directly proportional to the fourth power of the absolute temperature
The wave length corresponding to the maximum energy is proportional to the absolute temperature
The ratio of the emissive power and absorptive power of all bodies is the same and is equal to the emissive power of a perfectly black body
None of the above
Thermometer
Thermistor
Thermocouple
None of these
First law of thermodynamics
Newton's law of cooling
Newton's law of heating
Stefan's law
Irregular surfaces
Nonuniform temperature surfaces
One dimensional cases only
Two dimensional cases only
Maximum
Minimum
Zero
None of these
Their atoms collide frequently
Their atoms are relatively far apart
They contain free electrons
They have high density
tm = (Δt1 - Δt2)/ loge (Δt1/Δt2)
tm = loge (Δt1/Δt2)/ (Δt1 - Δt2)
tm = tm = (Δt1 - Δt2) loge (Δt1/Δt2)
tm = loge (Δt1 - Δt2)/ Δt1/Δt2
Zeroth law of thermodynamics
First law of thermodynamics
Second law of thermodynamics
Kirchhoff's law
Pb = pa - pv
Pb = pa + pv
Pb = pa × pv
Pb = pa/pv
Domestic refrigerators
Water coolers
Room air conditioners
All of these
W/m²K
W/m²
W/mK
W/m
Both the fluids at inlet (of heat exchanger where hot fluid enters) are in their coldest state
Both the fluids at inlet are in their hottest state
Both the fluids at exit are in their hottest state
One fluid is in hottest state and other in coldest state at inlet
Convection
Radiation
Forced convection
Free convection
Blast furnace
Heating of building
Cooling of parts in furnace
Heat received by a person from fireplace
Directly proportional to thermal conductivity
Inversely proportional to density of substance
Inversely proportional to specific heat
All of the above
Better insulation should be put over pipe and better one over it
Inferior insulation should be put over pipe and better one over it
Both may be put in any order
Whether to put inferior OIL over pipe or the better one would depend on steam temperature
Black body
Grey body
Opaque body
White body
Higher
Lower
Same
Depends upon the shape of body
Glass
Water
Plastic
Air
Fourier equation
Stefan-Boltzmann equation
Newton Reichmann equation
Joseph-Stefan equation
The heat transfer in liquid and gases takes place according to convection.
The amount of heat flow through a body is dependent upon the material of the body.
The thermal conductivity of solid metals increases with rise in temperature
Logarithmic mean temperature difference is not equal to the arithmetic mean temperature difference.
Conduction
Convection
Radiation
None of these
Shorter wavelength
Longer wavelength
Remain same at all wavelengths
Wavelength has nothing to do with it
Equal to
Directly proportional to
Inversely proportional to
None of these
Improve heat transfer
Provide support for tubes
Prevent stagnation of shell side fluid
All of these
Conduction
Convection
Radiation
Scattering