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
C. An equation relating pressure, volume and temperature of a gas is called ideal gas equation
Reversible isothermal volume change
Heating of a substance
Cooling of a substance
Simultaneous heating and expansion of an ideal gas
Moisture free ice
Solid helium
Solid carbon dioxide
None of these
Use of only one graph for all gases
Covering of wide range
Easier plotting
More accurate plotting
448
224
22.4
Data insufficient; can't be computed
+ve
-ve
0
Either of the above three; depends on the nature of refrigerant
Zero
Unity
Infinity
An indeterminate value
Only F decreases
Only A decreases
Both F and A decreases
Both F and A increase
The available energy in an isolated system for all irreversible (real) processes decreases
The efficiency of a Carnot engine increases, if the sink temperature is decreased
The reversible work for compression in non-flow process under isothermal condition is the change in Helmholtz free energy
All (A), (B) and (C)
Disorder
Orderly behaviour
Temperature changes only
None of these
Solution
Formation
Dilution
Combustion
Entropy
Internal energy
Enthalpy
Gibbs free energy
CO2
H2
O2
N2
Helmholtz
Gibbs
Both a & b
Neither 'a' nor 'b'
Reversible isothermal
Irreversible isothermal
Reversible adiabatic
None of these
Decreases
Increases
Remain same
Decreases linearly
Vapor pressure
Partial pressure
Chemical potential
None of these
Temperature
Specific heat
Volume
Pressure
4 J
∞
0
8 J
Enthalpies of all elements in their standard states are assumed to be zero
Combustion reactions are never endothermic in nature
Heat of reaction at constant volume is equal to the change in internal energy
Clausius-Clapeyron equation is not applicable to melting process
Enthalpy does not remain constant
Entire apparatus is exposed to surroundings
Temperature remains constant
None of these
Isothermal
Adiabatic
Isentropic
None of these
(∂T/∂V)S = (∂p/∂S)V
(∂T/∂P)S = (∂V/∂S)P
(∂P/∂T)V = (∂S/∂V)T
(∂V/∂T)P = -(∂S/∂P)T
Volume of the liquid phase is negligible compared to that of vapour phase
Vapour phase behaves as an ideal gas
Heat of vaporisation is independent of temperature
All (A), (B) & (C)
Temperature
Pressure
Composition
All (A), (B) and (C)
-273
0
-78
5
Specific heat
Latent heat of vaporisation
Viscosity
Specific vapor volume
The amount of work needed is path dependent
Work alone cannot bring out such a change of state
The amount of work needed is independent of path
More information is needed to conclude anything about the path dependence or otherwise of the work needed
Supersaturated
Superheated
Both (A) and (B)
Neither (A) nor (B)
First law
Zeroth law
Third law
Second law
Positive
Negative
Zero
May be positive or negative