Change vapour into liquid
Change liquid into vapour
Increase the temperature of a liquid of vapour
Convert water into steam and superheat it
C. Increase the temperature of a liquid of vapour
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
P = 0, x = 0 and a = 1
P=1, x = 0 and a = 0
P = 0, x = 1 and a = 0
X = 0, a + p = 1 Where a = absorptivity, p = reflectivity, X = transmissivity.
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
Equal to
Directly proportional to
Inversely proportional to
None of these
Added insulation will increase heat loss
Added insulation will decrease heat loss
Convective heat loss will be less than conductive heat loss
Heat flux will decrease
Wien's law
Planck's law
Stefan's law
Fourier's law
Change vapour into liquid
Change liquid into vapour
Increase the temperature of a liquid of vapour
Convert water into steam and superheat it
Electric heater
Steam condenser
Boiler
Refrigerator condenser coils
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 = 0 Where a = absorptivity, p = reflectivity, X = transmissivity.
Nature of the body
Temperature of the body
Type of surface of the body
All of these
Conduction
Free convection
Forced convection
Radiation
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
Pb = pa - pv
Pb = pa + pv
Pb = pa × pv
Pb = pa/pv
Conduction
Convection
Radiation
Conduction and convection
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
Grashoff number
Nusselt number
Weber number
Prandtl number
h₁ + h₂ + h₃
(h₁.h₂.h₃)1/3
1/h₁ + 1/h₂ + 1/h₃
None of these
Absolute temperature
T²
T⁵
T
Absorptive power
Emissive power
Emissivity
None of these
Grey body
Brilliant white polished body
Red hot body
Black body
Stanton number
Biot number
Peclet number
Grashoff number
Conduction
Convection
Radiation
Conduction and convection
Move actually
Do not move actually
Affect the intervening medium
Does not affect the intervening medium
Its temperature
Nature of the body
Kind and extent of its surface
All of the above
Cold body to hot body
Hot body to cold body
Smaller body to larger body
Larger body to smaller body
Melting of ice
Boiler furnaces
Condensation of steam in condenser
None of these
Glass
Water
Plastic
Air
Equal to one
Greater than one
Less than one
Equal to Nusselt number
Direct mixing of hot and cold fluids
A complete separation between hot and cold fluids
Flow of hot and cold fluids alternately over a surface
Generation of heat again and again
1 : 1
2 : 1
1 : 2
4 : 1