Universal gas constant
Kinematic viscosity
Thermal conductivity
Planck's constant
D. Planck's constant
Same
More
Less
Depends on other factors
The time taken to attain the final temperature to be measured
The time taken to attain 50% of the value of initial temperature difference
The time taken to attain 63.2% of the value of initial temperature difference
Determined by the time taken to reach 100°C from 0°C
Directly proportional to thermal conductivity
Inversely proportional to density of substance
Inversely proportional to specific heat
All of the above
J/m² sec
J/m °K sec
W/m °K
Option (B) and (C) above
Convection
Radiation
Forced convection
Free convection
Parallel flow type
Counter flow type
Cross flow type
Regenerator type
Move actually
Do not move actually
Affect the intervening medium
Does not affect the intervening medium
k₁ k₂
(k₁ + k₂)
(k₁ + k₂)/ k₁ k₂
2 k₁ k₂/ (k₁ + k₂)
-1/3
-2/3
1
-1
Wien's law
Planck's law
Stefan's law
Fourier's law
Face area
Time
Thickness
Temperature difference
A grey body is one which absorbs all radiations incident on it.
At thermal equilibrium, the emissivity and absorptivity are same.
The energy absorbed by a body to the total energy falling on it, is called emissivity.
A perfect body is one which is black in colour.
Increases
Decreases
Remain constant
May increase or decrease depending on temperature
α = 1, ρ = 0 and τ = 0
α = 0, ρ = 1 and τ = 0
α = 0, ρ = 0 and τ = 1
α + ρ = 1 and τ = 0
Minimum energy
Maximum energy
Both (A) and (B)
None of these
2 TR
4 TR
8 TR
10 TR
I.C. engine
Air preheaters
Heating of building in winter
None of the above
Absorptive power
Emissive power
Absorptivity
Emissivity
From one particle of the body to another without the actual motion of the particles
From one particle of the body to another by the actual motion of the heated particles
From a hot body to a cold body, in a straight line, without affecting the intervening medium
None of the above
Improve heat transfer
Provide support for tubes
Prevent stagnation of shell side fluid
All of these
Conduction
Convection
Radiation
Conduction and convection
Blast furnace
Heating of building
Cooling of parts in furnace
Heat received by a person from fireplace
0.1
0.3
0.7
1.7
Domestic refrigerators
Water coolers
Room air conditioners
All of these
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)
Radiators in automobile
Condensers and boilers in steam plants
Condensers and evaporators in refrigeration and air conditioning units
All of the above
At all temperatures
At one particular temperature
When system is under thermal equilibrium
At critical temperature
Quantity of heat flowing in one second through one cm cube of material when opposite faces ^re maintained at a temperature difference of 1°C
Quantity of heat flowing in one second through a slab of the material of area one cm square, thickness 1 cm when its faces differ in temperature by 1°C
Heat conducted in unit time across unit area through unit thickness when a temperature difference of unity is maintained between opposite faces
All of the above
Watt/mK
Watt/m²K²
Watt/m²K4
Watt/mK²
Black body
Grey body
Opaque body
White body