The energy change of a system undergoing any reversible process is zero
It is not possible to transfer heat from a lower temperature to a higher temperature
The total energy of system and surrounding remains the same
None of the above
D. None of the above
Trouton's ratio of non-polar liquids is calculated using Kistyakowsky equation
Thermal efficiency of a Carnot engine is always less than 1
An equation relating pressure, volume and temperature of a gas is called ideal gas equation
None of these
Isothermal
Irreversible
Adiabatic
Reversible
Increased COP
Same COP
Decreased COP
Increased or decreased COP; depending upon the type of refrigerant
Surface tension of a substance vanishes at critical point, as there is no distinction between liquid and vapour phases at its critical point
Entropy of a system decreases with the evolution of heat
Change of internal energy is negative for exothermic reactions
The eccentric factor for all materials is always more than one
35 K
174 K
274 K
154 K
448
224
22.4
Data insufficient; can't be computed
Less pronounced
More pronounced
Equal
Data insufficient, can't be predicted
Steam to ethylene ratio
Temperature
Pressure
None of these
Is zero
Increases
Decreases whereas the entropy increases
And entropy both decrease
Compressibility
Work done under adiabatic condition
Work done under isothermal condition
Co-efficient of thermal expansion
Pressure must be kept below 5.2 atm
Temperature must be kept above - 57°C
Pressure must be kept below 5.2 atm. and temperature must be kept above 57°C
Pressure and temperature must be kept below 5.2 atm. and - 57°C respectively
Isochoric
Isobaric
Adiabatic
Isothermal
Expansion of an ideal gas against constant pressure
Atmospheric pressure vaporisation of water at 100°C
Solution of NaCl in water at 50°C
None of these
By throttling
By expansion in an engine
At constant pressure
None of these
Critical properties
Specific gravity
Specific volume
Thermal conductivity
Molar concentration
Temperature
Internal energy
None of these
+ve
0
-ve
∞
Pressure and temperature
Reduced pressure and reduced temperature
Critical pressure and critical temperature
None of these
0.25
0.5
0.75
1
> 2
< 1
> 1
< 3
Entropy
Internal energy
Enthalpy
Gibbs free energy
Adiabatic process
Isothermal process
Isobaric process
All require same work
Free expansion of a gas
Compression of air in a compressor
Expansion of steam in a turbine
All (A), (B) & (C)
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)
Matter
Energy
Neither matter nor energy
Both matter and energy
Increase
Decrease
No change
None of these
Sub-cooled
Saturated
Non-solidifiable
None of these
Reverse Carnot cycle
Ordinary vapour-compression cycle
Vapour-compression process with a reversible expansion engine
Air refrigeration cycle
dQ = dE + dW
dQ = dE - dW
dE = dQ + dW
dW = dQ + dE
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)