6
9
27
81
D. 81
S.H/(S.H + L.H)
(S.H + L.H) /S.H
(L.H - S.H)/S.H
S.H/(L.H - S.H)
Shorter wavelength
Longer wavelength
Remain same at all wavelengths
Wavelength has nothing to do with it
Solids
Liquids
Gases
None of these
Iron
Lead
Concrete
Wood
Universal gas constant
Kinematic viscosity
Thermal conductivity
Planck's constant
Electric heater
Steam condenser
Boiler
Refrigerator condenser coils
Face area
Time
Thickness
Temperature difference
Cold water inlet and outlet
Hot medium inlet and outlet
Hot medium outlet and cold water inlet
Hot medium outlet and cold water outlet
Its temperature
Nature of the body
Kind and extent of its surface
All of the above
Thermal conductivity
Thermal diffusivity
Density
Dynamic viscosity
Nature of the body
Temperature of the body
Type of surface of the body
All of these
Improve heat transfer
Provide support for tubes
Prevent stagnation of shell side fluid
All of these
20°C
40°C
60°C
66.7°C
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
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)
Conduction
Convection
Radiation
None of these
Black body
Grey body
Opaque body
White body
Absorptive power
Emissive power
Absorptivity
Emissivity
I.C. engine
Air preheaters
Heating of building in winter
None of the above
1 : 1
2 : 1
1 : 2
4 : 1
Thermal coefficient
Thermal resistance
Thermal conductivity
None of these
Liquids
Energy
Temperature
Entropy
In conduction, reduction in the thickness of the material and an increase in thermal conductivity.
In convection, stirring of the fluid and cleaning the heating surface.
In radiation, increasing the temperature and reducing the emissivity.
All of the above
Conduction
Convection
Radiation
None of these
Is black in colour
Reflects all heat
Transmits all heat radiations
Absorbs heat radiations of all wave lengths falling on it
Fourier equation
Stefan-Boltzmann equation
Newton Reichmann equation
Joseph-Stefan equation
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
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.
Emissivity
Transmissivity
Reflectivity
Intensity of radiation
Pb = pa - pv
Pb = pa + pv
Pb = pa × pv
Pb = pa/pv