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
A. Better insulation should be put over pipe and better one over it
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.
P = 0, x = 0 and a = 1
P=1, x = 0, and a = 0
P = 0, T= 1, and a = 0
X = 0, a + p = 1
Directly proportional to the thermal conductivity
Inversely proportional to density of substance
Inversely proportional to specific heat
All of the above
Grashoff number
Nusselt number
Weber number
Prandtl number
Different heat contents
Different specific heat
Different atomic structure
Different temperatures
Parallel flow
Counter flow
Cross flow
All of these
Grey body
Brilliant white polished body
Red hot body
Black body
20°C
40°C
60°C
66.7°C
Higher
Lower
Same
Depends upon the shape of body
Convection
Radiation
Forced convection
Free convection
0.002
0.02
0.01
0.1
0.1
0.23
0.42
0.51
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.
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
Face area
Time
Thickness
Temperature difference
Glass
Water
Plastic
Air
Directly proportional to the surface area of the body
Directly proportional to the temperature difference on the two faces of the body
Dependent upon the material of the body
All of the above
Grashoff number
Biot number
Stanton number
Prandtl number
Absorptive power
Emissive power
Absorptivity
Emissivity
Velocity reduction method
Equal friction method
Static regains method
Dual or double method
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
Move actually
Do not move actually
Affect the intervening medium
Does not affect the intervening medium
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)
Its temperature
Nature of the body
Kind and extent of its surface
All of the above
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
Liquids
Energy
Temperature
Entropy
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
k₁ k₂
(k₁ + k₂)
(k₁ + k₂)/ k₁ k₂
2 k₁ k₂/ (k₁ + k₂)
Absolute temperature
Square of temperature
Fourth power of absolute temperature
Fourth power of temperature
High thickness of insulation
High vapour pressure
Less thermal conductivity insulator
A vapour seal