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
C. Thermal efficiency of a Carnot engine depends upon the properties of the working fluid besides the source & sink temperatures
Decrease in velocity
Decrease in temperature
Decrease in kinetic energy
Energy spent in doing work
580
640
1160
Data insufficient; can't be computed
Less pronounced
More pronounced
Equal
Data insufficient, can't be predicted
SO2
NH3
CCl2F2
C2H4Cl2
Adiabatic
Isometric
Isentropic
Isothermal
0.5
3.5
4.5
8.5
Less than
More than
Equal to or higher than
Less than or equal to
Enthalpy remains constant
Entropy remains constant
Temperature remains constant
None of these
Ice at the base contains impurities which lowers its melting point
Due to the high pressure at the base, its melting point reduces
The iceberg remains in a warmer condition at the base
All (A), (B) and (C)
Molar heat capacity
Internal energy
Viscosity
None of these
Kinematic viscosity
Work
Temperature
None of these
In an isothermal system, irreversible work is more than reversible work
Under reversible conditions, the adiabatic work is less than isothermal work
Heat, work, enthalpy and entropy are all 'state functions'
Matter and energy cannot be exchanged with the surroundings in a closed system
0
1
< 1
> 1
Binary solutions
Ternary solutions
Azeotropic mixture only
None of these
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
Ideal compression of air
Free expansion of an ideal gas
Adiabatic expansion of steam in a turbine
Adiabatic compression of a perfect gas
5 & 3
3.987 & 1.987
1.987 & 0.66
0.66 & 1.987
Chemical potential
Fugacity
Both (A) and (B)
Neither (A) nor (B)
Mass
Energy
Momentum
None of these
Increases
Decreases
Remains unchanged
Decreases linearly
Heat pump
Heat engine
Carnot engine
None of these
More
Less
Same
Data insufficient to predict
Zero
Negative
Very large compared to that for endothermic reaction
Not possible to predict
Below
At
Above
Either 'b' or 'c'
Enthalpy
Pressure
Entropy
None of these
-2 RT ln 0.5
-RT ln 0.5
0.5 RT
2 RT
Vapor compression cycle using expansion valve
Air refrigeration cycle
Vapor compression cycle using expansion engine
Carnot refrigeration cycle
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
+ve
-ve
0
Either of the above three; depends on the nature of refrigerant
Same as Carnot cycle
Same as reverse Carnot cycle
Dependent on the refrigerant's properties
The least efficient of all refrigeration processes