Volume, mass and number of moles
Free energy, entropy and enthalpy
Both (A) and (B)
None of these
C. Both (A) and (B)
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
Volume of the liquid phase is negligible compared to that of vapour phase
Vapour phase behaves as an ideal gas
Heat of vaporisation is independent of temperature
All (A), (B) & (C)
Process must be isobaric
Temperature must decrease
Process must be adiabatic
Both (B) and (C)
μi = (∂F/∂ni)T, P, ni
μi = (∂A/∂ni)T, P, ni
μi = (∂F/∂ni)T, P
μi = (∂A/∂ni)T, P
Like internal energy and enthalpy, the absolute value of standard entropy for elementary substances is zero
Melting of ice involves increase in enthalpy and a decrease in randomness
The internal energy of an ideal gas depends only on its pressure
Maximum work is done under reversible conditions
Departure from ideal solution behaviour
Departure of gas phase from ideal gas law
Vapour pressure of liquid
None of these
Rectangle
Rhombus
Trapezoid
Circle
4 J
∞
0
8 J
Trouton's ratio of non-polar liquids is calculated using Kistyakowsky equation
Thermal efficiency of a Carnot engine is always less than 1
An equation relating pressure, volume and temperature of a gas is called ideal gas equation
None of these
Melting of ice
Condensation of alcohol vapor
Sudden bursting of a cycle tube
Evaporation of water
Reaction mechanism
Calculation of rates
Energy transformation from one form to another
None of these
Reverse Carnot cycle
Ordinary vapour-compression cycle
Vapour-compression process with a reversible expansion engine
Air refrigeration cycle
TVγ-1 = constant
p1-γ.TY = constant
PVγ = constant
None of these
Enthalpy
Internal energy
Either (A) or (B)
Neither (A) nor (B)
0.15
1.5
4.5
6.5
Vant-Hoff equation
Le-Chatelier's principle
Arrhenius equation
None of these
First law
Zeroth law
Third law
Second law
Gibbs-Duhem equation
Gibbs-Helmholtz equation
Third law of thermodynamics
Joule-Thomson effect
Chemical potential
Surface tension
Heat capacity
None of these
-273
0
-78
5
(∂E/∂ni)S, v, nj
(∂G/∂ni)T, P, nj = (∂A/∂ni) T, v, nj
(∂H/∂ni)S, P, nj
All (A), (B) and (C)
Infinity
Minus infinity
Zero
None of these
Freon-12
Ethylene
Ammonia
Carbon dioxide
+ve
0
-ve
∞
Steam to ethylene ratio
Temperature
Pressure
None of these
+ve
-ve
0
Either of the above three; depends on the nature of refrigerant
Enthalpy
Entropy
Pressure
None of these
Entropy
Temperature
Internal energy
Enthalpy
Entropy
Gibbs free energy
Internal energy
All (A), (B) & (C)
Same in both the phases
Zero in both the phases
More in vapour phase
More in liquid phase