Conduction
Convection
Radiation
Conduction and convection
B. Convection
Energy transferred by convection to that by conduction
Kinematic viscosity to thermal diffusivity
Inertia force to viscous force
None of the above
Universal gas constant
Kinematic viscosity
Thermal conductivity
Planck's constant
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.
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
Convection
Radiation
Conduction and convection
Black body
Grey body
Opaque body
White body
k. A. (dT/dx)
k. A. (dx/dT)
k. (dT/dx)
k. (dx/dT)
Increases
Decreases
Remain constant
May increase or decrease depending on temperature
Cold water inlet and outlet
Hot medium inlet and outlet
Hot medium outlet and cold water inlet
Hot medium outlet and cold water outlet
Conduction
Convection
Radiation
Conduction and convection
-1/3
-2/3
1
-1
Change vapour into liquid
Change liquid into vapour
Increase the temperature of a liquid of vapour
Convert water into steam and superheat it
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
Moisture
Density
Temperature
All of the above
Parallel flow
Counter flow
Cross flow
All of these
Wien's law
Stefan's law
Kirchhoff's law
Planck's law
1 : 1
2 : 1
1 : 2
4 : 1
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.
0.002
0.02
0.01
0.1
Grashoff number
Biot number
Stanton number
Prandtl number
25 mm
40 mm
160 mm
800 mm
Conduction
Convection
Radiation
Scattering
Higher
Lower
Same
Depends on the area of heat exchanger
2 TR
4 TR
8 TR
10 TR
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
Solids
Liquids
Gases
None of these
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
Pb = pa - pv
Pb = pa + pv
Pb = pa × pv
Pb = pa/pv
Change vapour into liquid
Change liquid into vapour
Increase the temperature of a liquid or vapour
Convert water into steam and superheat it
k/h₀
2k/h₀
h₀/k
h₀/2k