Conduction
Convection
Radiation
None of these
B. Convection
Conduction
Free convection
Forced convection
Radiation
Stanton number
Biot number
Peclet number
Grashoff number
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
Absolute temperature
T²
T⁵
T
Nature of body
Temperature of body
Type of surface of body
All of the above
Change vapour into liquid
Change liquid into vapour
Increase the temperature of a liquid of vapour
Convert water into steam and superheat it
0.1
0.3
0.7
1.7
Higher
Lower
Same
Depends on the area of heat exchanger
Free electrons
Atoms colliding frequency
Low density
Porous body
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
Blast furnace
Heating of building
Cooling of parts in furnace
Heat received by a person from fireplace
Kirchoffs law
Stefan's law
Wien' law
Planck's law
Conduction
Convection
Radiation
None of these
Iron
Lead
Concrete
Wood
Universal gas constant
Kinematic viscosity
Thermal conductivity
Planck's constant
20°C
40°C
60°C
66.7°C
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
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
Improve heat transfer
Provide support for tubes
Prevent stagnation of shell side fluid
All of these
Shorter wavelength
Longer wavelength
Remain same at all wavelengths
Wavelength has nothing to do with it
Absorptive power
Emissive power
Absorptivity
Emissivity
The better insulation must be put inside
The better insulation must be put outside
One could place either insulation on either side
One should take into account the steam temperature before deciding as to which insulation is put where
Its temperature
Nature of the body
Kind and extent of its surface
All of the above
Zeroth law of thermodynamics
First law of thermodynamic
Second law of the thermodynamics
Kirchoff's law
Increase
Decrease
Remain unaffected
May increase/decrease depending on temperature and thickness of insulation
Increases
Decreases
Remain constant
May increase or decrease depending on temperature
Same
Less
Greater
None of these
h = k/ ρS
h = ρS/k
h = S/ρk
h = kρ/S
J/m² sec
J/m °K sec
W/m °K
Option (B) and (C) above
-1/3
-2/3
1
-1