Lewis-Randall
Margules
Van Laar
Both (B) & (C)
D. Both (B) & (C)
Amount of energy transferred
Direction of energy transfer
Irreversible processes only
Non-cyclic processes only
Low T, low P
High T, high P
Low T, high P
High T, low P
Equation of state
Gibbs Duhem equation
Ideal gas equation
None of these
< 0
> 0
= 0
None of these
-94 kcal
+94 kcal
> 94 kcal
< -94 kcal
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
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
0
1
2
3
Increases, for an exothermic reaction
Decreases, for an exothermic reaction
Increases, for an endothermic reaction
None of these
(∂E/∂T)V
(∂E/∂V)T
(∂E/∂P)V
(∂V/∂T)P
Below
At
Above
Either 'b' or 'c'
Isolated
Closed
Open
None of these
Tds = dE - dW = 0
dE - dW - Tds = 0
Tds - dE + dW < 0
Tds - dT + dW < 0
Prediction of the extent of a chemical reaction
Calculating absolute entropies of substances at different temperature
Evaluating entropy changes of chemical reaction
Both (B) and (C)
Chemical potential
Activity
Fugacity
Activity co-efficient
Temperature
Pressure
Composition
All (A), (B) and (C)
Any
A perfect
An easily liquefiable
A real
The concentration of each component should be same in the two phases
The temperature of each phase should be same
The pressure should be same in the two phases
The chemical potential of each component should be same in the two phases
Concentration
Mass
Temperature
Entropy
Van Laar
Margules
Gibbs-Duhem
Gibbs-Duhem-Margules
Bomb
Separating
Bucket
Throttling
Stirling
Brayton
Rankine
Both (B) and (C)
Low pressure & high temperature
High pressure & low temperature
Low pressure & low temperature
None of these
Gibbs-Duhem
Maxwell's
Clapeyron
None of these
349
651
667
1000
Isothermal
Adiabatic
Isentropic
None of these
Entropy
Gibbs free energy
Internal energy
All (A), (B) & (C)
Volume
Temperature
Pressure
None of these
(T2 - T1)/T2
(T2 - T1)/T1
(T1 - T2)/T2
(T1 - T2)/T1
Lowest
Highest
Average
None of these