Extensive property
Intensive property
Force which drives the chemical system to equilibrium
Both (B) and (C)
D. Both (B) and (C)
Non-flow reversible
Adiabatic
Both (A) and (B)
Neither (A) nor (B)
He
N2
O2
H2
Air cycle
Carnot cycle
Ordinary vapour compression cycle
Vapour compression with a reversible expansion engine
P ∝ 1/V, when temperature is constant
P ∝ 1/V, when temperature & mass of the gas remain constant
P ∝ V, at constant temperature & mass of the gas
P/V = constant, for any gas
Fugacity
Activity co-efficient
Free energy
All (A), (B) & (C)
Volume
Pressure
Temperature
All (A), (B) and (C)
Pressure
Solubility
Temperature
None of these
Isolated
Closed
Open
None of these
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)
Ideal
Very high pressure
Very low temperature
All of the above
3
1
2
0
High thermal conductivity
Low freezing point
Large latent heat of vaporisation
High viscosity
Zero
Positive
Negative
None of these
Number of intermediate chemical reactions involved
Pressure and temperature
State of combination and aggregation in the beginning and at the end of the reaction
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)
Bertholet equation
Clausius-Clapeyron equation
Beattie-Bridgeman equation
None of these
1
2
3
4
Solid-vapor
Solid-liquid
Liquid-vapor
All (A), (B) and (C)
Entropy
Internal energy
Enthalpy
Gibbs free energy
Heat capacity
Molal heat capacity
Pressure
Concentration
Pressure
Temperature
Both (A) & (B)
Neither (A) nor (B)
Matter
Energy
Neither matter nor energy
Both matter and energy
0
1
2
3
0
+ve
-ve
∞
Moisture free ice
Solid helium
Solid carbon dioxide
None of these
Isothermal
Adiabatic
Isobaric
Isometric
Decreases in all spontaneous (or irreversible) processes
Change during a spontaneous process has a negative value
Remains unchanged in reversible processes carried at constant temperature and pressure
All (A), (B) and (C)
Chemical potential
Activity
Fugacity
Activity co-efficient
Tds = dE - dW = 0
dE - dW - Tds = 0
Tds - dE + dW < 0
Tds - dT + dW < 0
Less
More
Same
More or less depending upon the extent of work done