Minimum energy
Maximum energy
Both (A) and (B)
None of these
B. Maximum energy
A dimensionless parameter
Function of temperature
Used as mathematical model
A physical property of the material
Cold water inlet and outlet
Hot medium inlet and outlet
Hot medium outlet and cold water inlet
Hot medium outlet and cold water outlet
h = k/ ρS
h = ρS/k
h = S/ρk
h = kρ/S
Zeroth law of thermodynamics
First law of thermodynamics
Second law of thermodynamics
Kirchhoff's law
Conduction
Convection
Radiation
None of these
Velocity reduction method
Equal friction method
Static regains method
Dual or double method
Directly proportional to thermal conductivity
Inversely proportional to density of substance
Inversely proportional to specific heat
All of the above
Increases
Decreases
Remain constant
May increase or decrease depending on temperature
Solids
Liquids
Gases
None of these
Liquids
Energy
Temperature
Entropy
Hr (time)
Sq. m (area)
°C (temperature)
K.cal (heat)
1 : 1
2 : 1
1 : 2
4 : 1
Thermal coefficient
Thermal resistance
Thermal conductivity
None of these
k₁ k₂
(k₁ + k₂)
(k₁ + k₂)/ k₁ k₂
2 k₁ k₂/ (k₁ + k₂)
Thermal resistance
Thermal coefficient
Temperature gradient
Thermal conductivity
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
Free electrons
Atoms colliding frequency
Low density
Porous body
6
9
27
81
Q = [2πlk (T₁ - T₂)]/2.3 log (r₂/r₁)
Q = 2.3 log (r₂/r₁)/[2πlk (T₁ - T₂)]
Q = [2π (T₁ - T₂)]/2.3 lk log (r₂/r₁)
Q = = 2πlk/2.3 (T₁ - T₂) log (r₂/r₁)
Watt/cm² °K
Watt/cm4 °K
Watt²/cm °K⁴
Watt/cm² °K⁴
Iron
Lead
Concrete
Wood
Radiators in automobile
Condensers and boilers in steam plants
Condensers and evaporators in refrigeration and air conditioning units
All of the above
Q = 2πkr1 r2 (T1 - T2)/ (r2 - r1)
Q = 4πkr1 r2 (T1 - T2)/ (r2 - r1)
Q = 6πkr1 r2 (T1 - T2)/ (r2 - r1)
Q = 8πkr1 r2 (T1 - T2)/ (r2 - r1)
Better insulation should be put over pipe and better one over it
Inferior insulation should be put over pipe and better one over it
Both may be put in any order
Whether to put inferior OIL over pipe or the better one would depend on steam temperature
Energy transferred by convection to that by conduction
Kinematic viscosity to thermal diffusivity
Inertia force to viscous force
None of the above
Grashoff number
Biot number
Stanton number
Prandtl number
Stanton number
Nusselt number
Biot number
Peclet number
Absolute temperature
T²
T⁵
T
Fourier equation
Stefan-Boltzmann equation
Newton Reichmann equation
Joseph-Stefan equation
Grey body
Brilliant white polished body
Red hot body
Black body