1 : 1
2 : 1
1 : 2
4 : 1
C. 1 : 2
Parallel flow type
Counter flow type
Cross flow type
Regenerator type
k. A. (dT/dx)
k. A. (dx/dT)
k. (dT/dx)
k. (dx/dT)
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
Electric heater
Steam condenser
Boiler
Refrigerator condenser coils
Blast furnace
Heating of building
Cooling of parts in furnace
Heat received by a person from fireplace
Thermal conductivity
Thermal diffusivity
Density
Dynamic viscosity
Grashoff number and Reynold number
Grashoff number and Prandtl number
Prandtl number and Reynold number
Grashoff number, Prandtl number and Reynold number
0
0.5
0.75
1
Directly proportional to the surface area
Directly proportional to the difference of temperatures between the two bodies
Either (A) or (B)
Both (A) and (B)
Absorptive power
Emissive power
Absorptivity
Emissivity
Steam
Solid ice
Melting ice
Water
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
Temperature
Thickness
Area
Time
Fourier equation
Stefan-Boltzmann equation
Newton Reichmann equation
Joseph-Stefan equation
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
h₁ + h₂ + h₃
(h₁.h₂.h₃)1/3
1/h₁ + 1/h₂ + 1/h₃
None of these
1 : 1
2 : 1
1 : 2
4 : 1
One dimensional cases only
Two dimensional cases only
Three dimensional cases only
Regular surfaces having non-uniform temperature gradients
S.H/(S.H + L.H)
(S.H + L.H) /S.H
(L.H - S.H)/S.H
S.H/(L.H - S.H)
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
Conduction
Free convection
Forced convection
Radiation
Different heat contents
Different specific heat
Different atomic structure
Different temperatures
Conduction
Convection
Radiation
None of these
Conduction
Convection
Radiation
None of these
Absolute temperature (T)
I²
F
T
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
Same
Higher
More or less same
Very much lower
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
Varies with temperature
Varies with the wave length of incident ray
Varies with both
Does not vary with temperature and wave length of the incident ray
Liquids
Energy
Temperature
Entropy