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
C. Flow of hot and cold fluids alternately over a surface
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)
h = k/ ρS
h = ρS/k
h = S/ρk
h = kρ/S
Conduction
Free convection
Forced convection
Radiation
Absolute temperature (T)
I²
F
T
Increases
Decreases
Remain constant
May increase or decrease depending on temperature
Wien's law
Planck's law
Stefan's law
Fourier's law
Minimum energy
Maximum energy
Both (A) and (B)
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
Increases
Decreases
Remain constant
May increase or decrease depending on temperature
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
Same
Higher
More or less same
Very much lower
0.1
0.23
0.42
0.51
Increases
Decreases
Remain constant
May increase or decrease depending on temperature
Hr (time)
Sq. m (area)
°C (temperature)
K.cal (heat)
Aluminium
Steel
Brass
Copper
0.1
0.3
0.7
1.7
A.Cmin/U
U/A.Cmin
A.U.Cmin
A.U/Cmin
Zeroth law of thermodynamics
First law of thermodynamic
Second law of the thermodynamics
Kirchoff's law
Parallel flow
Counter flow
Cross flow
All of these
Face area
Time
Thickness
Temperature difference
Conduction
Convection
Radiation
Conduction and convection
Blast furnace
Heating of building
Cooling of parts in furnace
Heat received by a person from fireplace
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
Absolute temperature
T²
T⁵
T
kcal/m²
kcal/hr °C
kcal/m² hr °C
kcal/m hr °C
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
Black body
Grey body
Opaque body
White body
Absolute temperature
Square of temperature
Fourth power of absolute temperature
Fourth power of temperature
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.
Thermal coefficient
Thermal resistance
Thermal conductivity
None of these