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
A. Thermal conductivity to the equivalent thickness of the film of fluid
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
Parallel flow type
Counter flow type
Cross flow type
Regenerator type
Conduction
Convection
Radiation
Conduction and convection
Change vapour into liquid
Change liquid into vapour
Increase the temperature of a liquid of vapour
Convert water into steam and superheat it
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
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
Conduction
Convection
Radiation
Conduction and convection
Black body
Grey body
Opaque body
White body
Fourier equation
Stefan-Boltzmann equation
Newton Reichmann equation
Joseph-Stefan equation
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
Scattering
Thermal resistance
Thermal coefficient
Temperature gradient
Thermal conductivity
Increases
Decreases
Remain constant
May increase or decrease depending on temperature
High thickness of insulation
High vapour pressure
Less thermal conductivity insulator
A vapour seal
20°C
40°C
60°C
66.7°C
k₁ k₂
(k₁ + k₂)
(k₁ + k₂)/ k₁ k₂
2 k₁ k₂/ (k₁ + k₂)
Grashoff number
Nusselt number
Weber number
Prandtl number
Velocity reduction method
Equal friction method
Static regains method
Dual or double method
Temperature
Thickness
Area
Time
Change vapour into liquid
Change liquid into vapour
Increase the temperature of a liquid or vapour
Convert water into steam and superheat it
Increases
Decreases
Remain constant
May increase or decrease depending on temperature
Watt/mK
Watt/m²K²
Watt/m²K4
Watt/mK²
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
h = k/ ρS
h = ρS/k
h = S/ρk
h = kρ/S
Their atoms collide frequently
Their atoms are relatively far apart
They contain free electrons
They have high density
Electric heater
Steam condenser
Boiler
Refrigerator condenser coils
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
A dimensionless parameter
Function of temperature
Used as mathematical model
A physical property of the material
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)
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