Entropy
Gibbs energy
Internal energy
Enthalpy
B. Gibbs energy
Negative
Zero
Infinity
None of these
Decreases
Increases
Remain same
May increase or decrease; depends on the nature of the gas
Adiabatic
Isothermal
Isometric
None of these
Decreases
Increases
Remains constant
Decreases logarithmically
Infinity
Minus infinity
Zero
None of these
Value of absolute entropy
Energy transfer
Direction of energy transfer
None of these
Infinity
Unity
Constant
Negative
Vapor pressure
Specific Gibbs free energy
Specific entropy
All (A), (B) and (C)
Contracts
Expands
Does not change in volume
Either (A), (B) or (C)
H = E - PV
H = F - TS
H - E = PV
None of these
Isothermal
Adiabatic
Isobaric
Isometric
More
Less
Same
Data insufficient to predict
Molecular size
Volume
Pressure
Temperature
Volume
Pressure
Temperature
All (A), (B) and (C)
At constant pressure
By throttling
By expansion in an engine
None of these
Departure from ideal solution behaviour
Departure of gas phase from ideal gas law
Vapour pressure of liquid
None of these
PV
2PV
PV/2
0
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)
μi = (∂F/∂ni)T, P, ni
μi = (∂A/∂ni)T, P, ni
μi = (∂F/∂ni)T, P
μi = (∂A/∂ni)T, P
Chemical potential
Surface tension
Heat capacity
None of these
Activity co-efficient is dimensionless.
In case of an ideal gas, the fugacity is equal to its pressure.
In a mixture of ideal gases, the fugacity of a component is equal to the partial pressure of the component.
The fugacity co-efficient is zero for an ideal gas
Not liquify (barring exceptions)
Immediately liquify
Never liquify however high the pressure may be
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
Stirling
Brayton
Rankine
None of these
Enthalpy
Volume
Both 'a' & 'b'
Neither 'a' nor 'b'
Volume
Pressure
Temperature
All a, b & c
0
1
2
3
Solid-vapor
Solid-liquid
Liquid-vapor
All (A), (B) and (C)
Molar concentration
Temperature
Internal energy
None of these
Low temperature
High pressure
Both (A) and (B)
Neither (A) nor (B)