Concentration
Mass
Temperature
Entropy
D. Entropy
Below
At
Above
Either 'b' or 'c'
A gas may have more than one inversion temperatures
The inversion temperature is different for different gases
The inversion temperature is same for all gases
The inversion temperature is the temperature at which Joule-Thomson co-efficient is infinity
Decrease in temperature
Increase in temperature
No change in temperature
Change in temperature which is a function of composition
Zero
Unity
Infinity
Negative
Pressure
Volume
Temperature
All (A), (B) and (C)
Less than
More than
Same as
Not related to
1st
Zeroth
3rd
None of these
Gibbs-Duhem
Maxwell's
Clapeyron
None of these
Lowest
Highest
Average
None of these
Rate of change of vapour pressure with temperature
Effect of an inert gas on vapour pressure
Calculation of ΔF for spontaneous phase change
Temperature dependence of heat of phase transition
0.25
0.5
0.75
1
Extensive property
Intensive property
Force which drives the chemical system to equilibrium
Both (B) and (C)
The values of (∂P/∂V)T and (∂2P/∂V2)T are zero for a real gas at its critical point
Heat transferred is equal to the change in the enthalpy of the system, for a constant pressure, non-flow, mechanically reversible process
Thermal efficiency of a Carnot engine depends upon the properties of the working fluid besides the source & sink temperatures
During a reversible adiabatic process, the entropy of a substance remains constant
Entropy
Gibbs energy
Internal energy
Enthalpy
Same as Carnot cycle
Same as reverse Carnot cycle
Dependent on the refrigerant's properties
The least efficient of all refrigeration processes
Zero
Unity
Infinity
None of these
RT d ln P
R d ln P
R d ln f
None of these
Latent heat of vaporisation
Chemical potential
Molal boiling point
Heat capacity
Same in both the phases
Zero in both the phases
More in vapour phase
More in liquid phase
Vapor pressure
Partial pressure
Chemical potential
None of these
Eutectic
Triple
Plait
Critical
Third law of thermodynamics
Second law of thermodynamics
Nernst heat theorem
Maxwell's relations
2.73
28.3
273
283
Heat capacity of a crystalline solid is zero at absolute zero temperature
Heat transfer from low temperature to high temperature source is not possible without external work
Gases having same reduced properties behaves similarly
None of these
Temperature
Pressure
Composition
All (A), (B) and (C)
72
92
142
192
dQ = dE + dW
dQ = dE - dW
dE = dQ + dW
dW = dQ + dE
Low pressure and high temperature
Low pressure and low temperature
High pressure and low temperature
High pressure and high temperature
Pressure
Volume
Mass
None of these
Heat absorbed
Work done
Both (A) & (B)
Neither (A) nor (B)