Reversible isothermal
Irreversible isothermal
Reversible adiabatic
None of these
C. Reversible adiabatic
Conduction
Convection
Radiation
Condensation
270
327
300
540
Unity
Activity
Both (A) & (B)
Neither (A) nor (B)
The net change in entropy in any reversible cycle is always zero
The entropy of the system as a whole in an irreversible process increases
The entropy of the universe tends to a maximum
The entropy of a substance does not remain constant during a reversible adiabatic change
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)
< 0
> 0
= 0
None of these
Violates second law of thermodynamics
Involves transfer of heat from low temperature to high temperature
Both (A) and (B)
Neither (A) nor (B)
The expansion of a gas in vacuum is an irreversible process
An isometric process is a constant pressure process
Entropy change for a reversible adiabatic process is zero
Free energy change for a spontaneous process is negative
Decrease on addition of Cl2
Increase on addition of an inert gas at constant pressure
Decrease on increasing the pressure of the system
None of these
A refrigeration cycle violates the second law of thermodynamics
Refrigeration cycle is normally represented by a temperature vs. entropy plot
In a refrigerator, work required decreases as the temperature of the refrigerator and the temperature at which heat is rejected increases
One ton of refrigeration is equivalent to the rate of heat absorption equal to 3.53 kW
Increase the partial pressure of H2
Increase the partial pressure of I2
Increase the total pressure and hence shift the equilibrium towards the right
Not affect the equilibrium conditions
0°C
273°C
100°C
-273°C
It should be non-explosive
It should have a sub-atmospheric vapor pressure at the temperature in refrigerator coils
Its vapor pressure at the condenser temperature should be very high
None of these
(∂P/∂V)S = (∂P/∂V)T
(∂P/∂V)S = [(∂P/∂V)T]Y
(∂P/∂V)S = y(∂P/∂V)T
(∂P/∂V)S = 1/y(∂P/∂V)T
Chemical potential
Activity
Fugacity
Activity co-efficient
0.25
0.5
0.75
1
Amount of energy transferred
Direction of energy transfer
Irreversible processes only
Non-cyclic processes only
Minimum
Zero
Maximum
None of these
Sub-cooled
Saturated
Non-solidifiable
None of these
Henry's law
Law of mass action
Hess's law
None of these
Pressure to critical pressure
Critical pressure to pressure
Pressure to pseudocritical pressure
Pseudocritical pressure to pressure
J/s
J.S
J/kmol
kmol/J
Phase rule variables are intensive properties
Heat and work are both state function
The work done by expansion of a gas in vacuum is zero
CP and CV are state function
Minimum temperature attainable
Temperature of the heat reservoir to which a Carnot engine rejects all the heat that is taken in
Temperature of the heat reservoir to which a Carnot engine rejects no heat
None of these
Bucket
Throttling
Separating
A combination of separating & throttling
Stirling
Brayton
Rankine
None of these
1st
Zeroth
3rd
None of these
Decreases
Increases
Remain same
May increase or decrease; depends on the nature of the gas
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
Molar volume, density, viscosity and boiling point
Refractive index and surface tension
Both (A) and (B)
None of these