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
A. tm = (Δt1 - Δt2)/ loge (Δt1/Δt2)
Higher
Lower
Same
Depends upon the shape of body
Increases
Decreases
Remain constant
May increase or decrease depending on temperature
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
Cold body to hot body
Hot body to cold body
Smaller body to larger body
Larger body to smaller body
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.
Radiators in automobile
Condensers and boilers in steam plants
Condensers and evaporators in refrigeration and air conditioning units
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
Nature of the body
Temperature of the body
Type of surface of the body
All of these
Conduction
Convection
Radiation
None of these
Zeroth law of thermodynamics
First law of thermodynamic
Second law of the thermodynamics
Kirchoff's law
Their atoms collide frequently
Their atoms are relatively far apart
They contain free electrons
They have high density
Face area
Time
Thickness
Temperature difference
2 TR
4 TR
8 TR
10 TR
Black body
Grey body
Opaque body
White body
Emissivity
Transmissivity
Reflectivity
Intensity of radiation
First law of thermodynamics
Newton's law of cooling
Newton's law of heating
Stefan's law
Parallel flow type
Counter flow type
Cross flow type
Regenerator type
Conduction
Free convection
Forced convection
Radiation
kcal/m²
kcal/hr °C
kcal/m² hr °C
kcal/m hr °C
S.H/(S.H + L.H)
(S.H + L.H) /S.H
(L.H - S.H)/S.H
S.H/(L.H - S.H)
Thermal conductivity
Thermal diffusivity
Density
Dynamic viscosity
Absolute temperature (T)
I²
F
T
Irregular surfaces
Nonuniform temperature surfaces
One dimensional cases only
Two dimensional cases only
Wien's law
Planck's law
Stefan's law
Fourier's law
25 mm
40 mm
160 mm
800 mm
0.45
0.55
0.40
0.75
Iron
Lead
Concrete
Wood
In heat exchanger design as a safety factor
In case of Newtonian fluids
When a liquid exchanges heat with a gas
None of the above
Solids
Liquids
Gases
None of these
Convection
Radiation
Conduction
Both convection and conduction