Energy transferred by convection to that by conduction
Kinematic viscosity to thermal diffusivity
Inertia force to viscous force
None of the above
C. Inertia force to viscous force
Nature of body
Temperature of body
Type of surface of body
All of the above
Thermal conductivity to the equivalent thickness of the film of fluid
Temperature drop through the films of fluids to the thickness of film of fluids
Thickness of film of fluid to the thermal conductivity
Thickness of film of fluid to the temperature drop through the films of fluids
2 TR
4 TR
8 TR
10 TR
Iron
Lead
Concrete
Wood
K cal/kg m² °C
K cal m/hr m² °C
K cal/hr m² °C
K calm/hr °C
0.1
0.23
0.42
0.51
Change vapour into liquid
Change liquid into vapour
Increase the temperature of a liquid of vapour
Convert water into steam and superheat it
Thermometer
Thermistor
Thermocouple
None of these
Cold water inlet and outlet
Hot medium inlet and outlet
Hot medium outlet and cold water inlet
Hot medium outlet and cold water outlet
Black radiation
Full radiation
Total radiation
All of these
kcal/m²
kcal/hr °C
kcal/m² hr °C
kcal/m hr °C
6
9
27
81
Pb = pa - pv
Pb = pa + pv
Pb = pa × pv
Pb = pa/pv
Convection
Radiation
Conduction
Both convection and conduction
Emissivity
Transmissivity
Reflectivity
Intensity of radiation
Conduction
Convection
Radiation
Conduction and convection
1 : 1
2 : 1
1 : 2
4 : 1
m²/hr
m²/hr °C
kcal/m² hr
kcal/m. hr °C
Increases
Decreases
Remain constant
May increase or decrease depending on temperature
It is impossible to transfer heat from low temperature source to t high temperature source
Heat transfer by radiation requires no medium
All bodies above absolute zero emit radiation
Heat transfer in most of the cases takes place by combination of conduction, convection and radiation
Function of temperature
Physical property of a substance
Dimensionless parameter
All of these
Domestic refrigerators
Water coolers
Room air conditioners
All of these
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
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
k/h₀
2k/h₀
h₀/k
h₀/2k
First law of thermodynamics
Newton's law of cooling
Newton's law of heating
Stefan's law
Solids
Liquids
Gases
None of these
Convection
Radiation
Forced convection
Free convection
Absolute temperature
T²
T⁵
T
Hr (time)
Sq. m (area)
°C (temperature)
K.cal (heat)