Higher
Lower
Same
Depends upon the shape of body
B. Lower
Varies with temperature
Varies with the wave length of incident ray
Varies with both
Does not vary with temperature and wave length of the incident ray
Improve heat transfer
Provide support for tubes
Prevent stagnation of shell side fluid
All of these
Blast furnace
Heating of building
Cooling of parts in furnace
Heat received by a person from fireplace
0.45
0.55
0.40
0.75
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
At all temperatures
At one particular temperature
When system is under thermal equilibrium
At critical temperature
Liquids
Energy
Temperature
Entropy
Function of temperature
Physical property of a substance
Dimensionless parameter
All of these
tm = (Δt1 - Δt2)/ loge (Δt1/Δt2)
tm = loge (Δt1/Δt2)/ (Δt1 - Δt2)
tm = tm = (Δt1 - Δt2) loge (Δt1/Δt2)
tm = loge (Δt1 - Δt2)/ Δt1/Δt2
Glass
Water
Plastic
Air
-1/3
-2/3
1
-1
Conduction
Convection
Radiation
Conduction and convection
More than those for liquids
Less than those for liquids
More than those for solids
Dependent on the viscosity
Grashoff number
Nusselt number
Weber number
Prandtl number
Grashoff number
Biot number
Stanton number
Prandtl number
Conduction
Convection
Radiation
None of these
Convection
Radiation
Forced convection
Free convection
Conduction
Convection
Radiation
None of these
Nature of body
Temperature of body
Type of surface of body
All of the above
Conduction
Convection
Radiation
None of these
Zeroth law of thermodynamics
First law of thermodynamics
Second law of thermodynamics
Kirchhoff's law
The total radiation from a black body per second per unit area is directly proportional to the fourth power of the absolute temperature
The wave length corresponding to the maximum energy is proportional to the absolute temperature
The ratio of the emissive power and absorptive power of all bodies is the same and is equal to the emissive power of a perfectly black body
None of the above
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.
Conduction
Free convection
Forced convection
Radiation
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
Minimum energy
Maximum energy
Both (A) and (B)
None of these
Convection
Radiation
Conduction
Both convection and conduction
Steam
Solid ice
Melting ice
Water
Parallel flow type
Counter flow type
Cross flow type
Regenerator type
Same
Less
Greater
None of these