Rate of heat transmission
Initial state only
End states only
None of these
C. End states only
Work done under adiabatic condition
Co-efficient of thermal expansion
Compressibility
None of these
Stirling
Brayton
Rankine
None of these
0
1
2
3
Free energy
Entropy
Refractive index
None of these
Enthalpy
Volume
Both 'a' & 'b'
Neither 'a' nor 'b'
0
1
2
3
Heat pump
Heat engine
Carnot engine
None of these
An ideal liquid or solid solution is defined as one in which each component obeys Raoult's law
If Raoult's law is applied to one component of a binary mixture; Henry's law or Raoult's law is applied to the other component also
Henry's law is rigorously correct in the limit of infinite dilution
None of these
Increase
Decrease
Not alter
None of these
Constant volume
Polytropic
Adiabatic
Constant pressure
Volume
Density
Temperature
Pressure
Independent of pressure
Independent of temperature
Zero at absolute zero temperature for a perfect crystalline substance
All (A), (B) & (C)
Molten sodium
Molten lead
Mercury
Molten potassium
Zero
50%
Almost 100%
unpredictable
Single phase fluid of varying composition
Single phase fluid of constant composition
Open as well as closed systems
Both (B) and (C)
T
√T
T2
1/√T
Adiabatic
Isothermal
Isometric
None of these
Sublimation
Fusion
Transition
Vaporisation
CV
Entropy change
Gibbs free energy
None of these
(∂P/∂V)S = (∂P/∂V)T
(∂P/∂V)S = [(∂P/∂V)T]Y
(∂P/∂V)S = y(∂P/∂V)T
(∂P/∂V)S = 1/y(∂P/∂V)T
Solubility increases as temperature increases
Solubility increases as temperature decreases
Solubility is independent of temperature
Solubility increases or decreases with temperature depending on the Gibbs free energy change of solution
Less than
Equal to
More than
Either (B) or (C); depends on the type of alloy
Latent heat of vaporisation
Chemical potential
Molal boiling point
Heat capacity
Work required to refrigeration obtained
Refrigeration obtained to the work required
Lower to higher temperature
Higher to lower temperature
d ln p/dt = Hvap/RT2
d ln p/dt = RT2/Hvap
dp/dt = RT2/Hvap
dp/dt = Hvap/RT2
F = A + PV
F = E + A
F = A - TS
F = A + TS
P ∝ 1/V, when temperature is constant
P ∝ 1/V, when temperature & mass of the gas remain constant
P ∝ V, at constant temperature & mass of the gas
P/V = constant, for any gas
Surface tension of a substance vanishes at critical point, as there is no distinction between liquid and vapour phases at its critical point
Entropy of a system decreases with the evolution of heat
Change of internal energy is negative for exothermic reactions
The eccentric factor for all materials is always more than one
μ° + RT ln f
μ°+ R ln f
μ° + T ln f
μ° + R/T ln f
CV
Enthalpy change
Free energy change
None of these