Joule-Thomson co-efficient
Specific heat at constant pressure (Cp)
co-efficient of thermal expansion
Specific heat at constant volume (CV)
C. co-efficient of thermal expansion
Increases
Decreases
Remains unchanged
First decreases and then increases
Shift the equilibrium towards right
Give higher yield of NH3
Both (B) and (C)
Neither (A) nor (B)
Cv.dT
Cp.dT
∫ Cp.dT
∫ Cv.dT
+ve
-ve
0
∞
Increases with increase in pressure
Decreases with increase in temperature
Is independent of temperature
None of these
Negative
Zero
Infinity
None of these
Low temperature and high pressure
Low temperature and low pressure
High temperature and high pressure
High temperature and low pressure
72
92
142
192
(dF)T, p <0
(dF)T, p = 0
(dF)T, p > 0
(dA)T, v >0
Mole fraction
Fugacity at the same temperature and pressure
Partial pressure
None of these
μi = (∂F/∂ni)T, P, ni
μi = (∂A/∂ni)T, P, ni
μi = (∂F/∂ni)T, P
μi = (∂A/∂ni)T, P
Increased COP
Same COP
Decreased COP
Increased or decreased COP; depending upon the type of refrigerant
Volume, mass and number of moles
Free energy, entropy and enthalpy
Both (A) and (B)
None of these
Fusion
Vaporisation
Transition
None of these
CV
Enthalpy change
Free energy change
None of these
300 × (32/7)
300 × (33/5)
300 × (333/7)
300 × (35/7)
0
1
2
3
Is the analog of linear frictionless motion in machines
Is an idealised visualisation of behaviour of a system
Yields the maximum amount of work
Yields an amount of work less than that of a reversible process
Zero
Negative
Very large compared to that for endothermic reaction
Not possible to predict
Critical temperature
Melting point
Freezing point
Both (B) and (C)
Unity
Zero
That of the heat of reaction
Infinity
Entropy and enthalpy are path functions
In a closed system, the energy can be exchanged with the surrounding, while matter cannot be exchanged
All the natural processes are reversible in nature
Work is a state function
Mass
Momentum
Energy
None of these
Minimum
Zero
Maximum
Indeterminate
Zero
Unity
Infinity
An indeterminate value
12 P1V1
6 P1 V1
3 P1V1
P1 V1
2
0
3
1
Increase the partial pressure of I2
Decrease the partial pressure of HI
Diminish the degree of dissociation of HI
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
3
2
1
0