Mole fraction
Fugacity at the same temperature and pressure
Partial pressure
None of these
A. Mole fraction
Less than
Same as
More than
Half
Two temperatures only
Pressure of working fluid
Mass of the working fluid
Mass and pressure both of the working fluid
Minimum
Zero
Maximum
None of these
Reversible
Irreversible
Isothermal
Adiabatic
Heat
Momentum
Energy
Work
Minimum number of degree of freedom of a system is zero
Degree of freedom of a system containing a gaseous mixture of helium, carbon dioxide and hydrogen is 4
For a two phase system in equilibrium made up of four non-reacting chemical species, the number of degrees of freedom is 4
Enthalpy and internal energy change is zero during phase change processes like melting, vaporisation and sublimation
RT ln K
-RT ln K
-R ln K
T ln K
Enthalpy
Entropy
Pressure
None of these
Two different gases behave similarly, if their reduced properties (i.e. P, V and T) are same
The surface of separation (i. e. the meniscus) between liquid and vapour phase disappears at the critical temperature
No gas can be liquefied above the critical temperature, howsoever high the pressure may be.
The molar heat of energy of gas at constant volume should be nearly constant (about 3 calories)
(atm)Δx, when Δx is negative
(atm)Δx, when Δx is positive
Dimensionless, when Δx = 0
(atm)Δx2, when Δx > 0
Heat absorbed
Work done
Both (A) & (B)
Neither (A) nor (B)
(dF)T, p <0
(dF)T, p = 0
(dF)T, p > 0
(dA)T, v >0
Sublimation
Vaporisation
Melting
Either (A), (B) or (C)
Unity
Zero
That of the heat of reaction
Infinity
Same in both the phases
Zero in both the phases
More in vapour phase
More in liquid phase
Increases
Decreases
Remains unchanged
Decreases linearly
Critical temperature
Melting point
Freezing point
Both (B) and (C)
The available energy in an isolated system for all irreversible (real) processes decreases
The efficiency of a Carnot engine increases, if the sink temperature is decreased
The reversible work for compression in non-flow process under isothermal condition is the change in Helmholtz free energy
All (A), (B) and (C)
349
651
667
1000
Fugacity
Activity co-efficient
Free energy
All (A), (B) & (C)
0
1
2
3
[∂(G/T)/∂T] = - (H/T2)
[∂(A/T)/∂T]V = - E/T2
Both (A) and (B)
Neither (A) nor (B)
∞
0
< 0
> 0
Lowest
Highest
Average
None of these
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
1
2
3
4
He
N2
O2
H2
At low temperature and high pressure
At standard state
Both (A) and (B)
In ideal state
Isothermally
Isobarically
Adiabatically
None of these
Less than
More than
Same as
Not related to