Reflected
Refracted
Transmitted
Absorbed
D. Absorbed
Irregular surfaces
Nonuniform temperature surfaces
One dimensional cases only
Two dimensional cases only
Domestic refrigerators
Water coolers
Room air conditioners
All of these
Conduction
Convection
Radiation
Conduction and convection
At all temperatures
At one particular temperature
When system is under thermal equilibrium
At critical temperature
Higher
Lower
Same
Depends upon the shape of body
Glass
Water
Plastic
Air
P = 0, x = 0 and a = 1
P=1, x = 0 and a = 0
P = 0, x = 1 and a = 0
X = 0, a + p = 1 Where a = absorptivity, p = reflectivity, X = transmissivity.
RN = hl/k
RN = μ cp/k
RN = ρ V l /μ
RN = V²/t.cp
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
Thermal resistance
Thermal coefficient
Temperature gradient
Thermal conductivity
Cold water inlet and outlet
Hot medium inlet and outlet
Hot medium outlet and cold water inlet
Hot medium outlet and cold water outlet
K cal/kg m² °C
K cal m/hr m² °C
K cal/hr m² °C
K calm/hr °C
Universal gas constant
Kinematic viscosity
Thermal conductivity
Planck's constant
From one particle of the body to another without the actual motion of the particles
From one particle of the body to another by the actual motion of the heated particles
From a hot body to a cold body, in a straight line, without affecting the intervening medium
None of the above
2 TR
4 TR
8 TR
10 TR
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)
0
0.5
0.75
1
Absorptive power
Emissive power
Absorptivity
Emissivity
First law of thermodynamics
Newton's law of cooling
Newton's law of heating
Stefan's law
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
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.
Zeroth law of thermodynamics
First law of thermodynamic
Second law of the thermodynamics
Kirchoff's law
The better insulation must be put inside
The better insulation must be put outside
One could place either insulation on either side
One should take into account the steam temperature before deciding as to which insulation is put where
Thermal coefficient
Thermal resistance
Thermal conductivity
None of these
Is black in colour
Reflects all heat
Transmits all heat radiations
Absorbs heat radiations of all wave lengths falling on it
Kirchhoff's law
Stefan's law
Wines law
Planck's law
Conduction
Convection
Radiation
Conduction and convection
Conduction
Convection
Radiation
Conduction and radiation combined
Watt/mK
Watt/m²K²
Watt/m²K4
Watt/mK²
Zeroth law of thermodynamics
First law of thermodynamics
Second law of thermodynamics
Kirchhoff's law