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
D. All 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.
Directly proportional to the thermal conductivity
Inversely proportional to density of substance
Inversely proportional to specific heat
All of the above
At all temperatures
At one particular temperature
When system is under thermal equilibrium
At critical temperature
Conduction
Convection
Radiation
None of these
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)
Cold water inlet and outlet
Hot medium inlet and outlet
Hot medium outlet and cold water inlet
Hot medium outlet and cold water outlet
Irregular surfaces
Nonuniform temperature surfaces
One dimensional cases only
Two dimensional cases only
Melting of ice
Boiler furnaces
Condensation of steam in condenser
None of these
Conduction
Convection
Radiation
Conduction and convection
High thickness of insulation
High vapour pressure
Less thermal conductivity insulator
A vapour seal
Conduction
Free convection
Forced convection
Radiation
Less than those for gases
Less than those for liquids
More than those for liquids and gases
More or less same as for liquids and gases
1 : 1
2 : 1
1 : 2
4 : 1
Temperature
Thickness
Area
Time
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)
Absolute temperature
Square of the absolute temperature
Cube of the absolute temperature
Fourth power of the absolute temperature
One dimensional cases only
Two dimensional cases only
Three dimensional cases only
Regular surfaces having non-uniform temperature gradients
Absorptive power
Emissive power
Absorptivity
Emissivity
Stanton number
Nusselt number
Biot number
Peclet number
Stanton number
Biot number
Peclet number
Grashoff number
Black radiation
Full radiation
Total radiation
All of these
Their atoms collide frequently
Their atoms are relatively far apart
They contain free electrons
They have high density
kcal/m²
kcal/hr °C
kcal/m² hr °C
kcal/m hr °C
Cold body to hot body
Hot body to cold body
Smaller body to larger body
Larger body to smaller body
Increases
Decreases
Remain constant
May increase or decrease depending on temperature
Liquids
Energy
Temperature
Entropy
Same
Less
Greater
None of these
0.002
0.02
0.01
0.1
Density
Coefficient of viscosity
Gravitational force
All of these
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