Increase
Decrease
No change
None of these
A. Increase
0
1
< 1
> 1
1
2
3
0
0
< 0
< 1
> 1
Concentration
Mass
Temperature
Entropy
Non-uniformly
Adiabatically
Isobarically
Isothermally
Directly proportional to pressure
Inversely proportional to pressure
Unity at all pressures
None of these
Entropy
Temperature
Enthalpy
Pressure
A closed system does not permit exchange of mass with its surroundings but may permit exchange of energy.
An open system permits exchange of both mass and energy with its surroundings
The term microstate is used to characterise an individual, whereas macro-state is used to designate a group of micro-states with common characteristics
None of the above
Contracts
Expands
Does not change in volume
Either (A), (B) or (C)
Vapor pressure
Specific Gibbs free energy
Specific entropy
All (A), (B) and (C)
0
∞
50
100
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)
Does not depend upon temperature
Is independent of pressure only
Is independent of volume only
Is independent of both pressure and volume
Lewis-Randall rule
Statement of Van't Hoff Equation
Le-Chatelier's principle
None of these
Escaping tendencies of the same substance in different phases of a system
Relative volatility of a mixture of two miscible liquids
Behaviour of ideal gases
None of these
0
273
25
None of these
0
1
2
3
Snow melts into water
A gas expands spontaneously from high pressure to low pressure
Water is converted into ice
Both (B) & (C)
dP/dT = ΔH/TΔV
ln P = - (ΔH/RT) + constant
ΔF = ΔH + T [∂(ΔF)/∂T]P
None of these
Equation of state
Gibbs Duhem equation
Ideal gas equation
None of these
ΔF = ΔH + T [∂(ΔF)/∂T]P
ΔF = ΔH - TΔT
d(E - TS) T, V < 0
dP/dT = ΔHvap/T.ΔVvap
Rate of change of vapour pressure with temperature
Effect of an inert gas on vapour pressure
Calculation of ΔF for spontaneous phase change
Temperature dependence of heat of phase transition
μi = (∂F/∂ni)T, P, ni
μi = (∂A/∂ni)T, P, ni
μi = (∂F/∂ni)T, P
μi = (∂A/∂ni)T, P
P + F - C = 2
C = P - F + 2
F = C - P - 2
P = F - C - 2
The surface tension vanishes
Liquid and vapour have the same density
There is no distinction between liquid and vapour phases
All (A), (B) and (C)
R loge 4
R log10 4
Cv log10 4
Cv loge 4
Specific heat at constant pressure (Cp)
Specific heat at constant volume (Cv)
Joule-Thompson co-efficient
None of these
Work done under adiabatic condition
Co-efficient of thermal expansion
Compressibility
None of these
None of these
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