Volume
Mass
Critical temperature
None of these
D. None of these
Compression ratio of an Otto engine is comparatively higher than a diesel engine
Efficiency of an Otto engine is higher than that of a diesel engine for the same compression ratio
Otto engine efficiency decreases with the rise in compression ratio, due to decrease in work produced per quantity of heat
Diesel engine normally operates at lower compression ratio than an Otto engine for an equal output of work
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
Free expansion of a gas
Compression of air in a compressor
Expansion of steam in a turbine
All (A), (B) & (C)
Closed
Open
Isolated
Non-thermodynamic
More
Less
Same
More or less; depending on the system
V1/V2
V2/V1
V1 - V2
V1.V2
Negative
Zero
Infinity
None of these
μi = (∂F/∂ni)T, P, ni
μi = (∂A/∂ni)T, P, ni
μi = (∂F/∂ni)T, P
μi = (∂A/∂ni)T, P
Pressure
Temperature
Both (A) & (B)
Neither (A) nor (B)
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
Snow melts into water
A gas expands spontaneously from high pressure to low pressure
Water is converted into ice
Both (B) & (C)
Becomes zero
Becomes infinity
Equals 1 kcal/kmol °K
Equals 0.24 kcal/kmol °K
Phase rule variables are intensive properties
Heat and work are both state function
The work done by expansion of a gas in vacuum is zero
CP and CV are state function
Pressure
Volume
Mass
None of these
System (of partially miscible liquid pairs), in which the mutual solubility increases with rise in temperature, are said to possess an upper consolute temperature
Systems, in which the mutual solubility increases with decrease in temperature, are said to possess lower consolute temperature
Nicotine-water system shows both an upper as well as a lower consolute temperature, implying that they are partially miscible between these two limiting temperatures
None of these
None of these
Critical
Boyle
Inversion
Reduced
Critical temperature
Melting point
Freezing point
Both (B) and (C)
Latent heat of vaporisation
Chemical potential
Molal boiling point
Heat capacity
Molar volume, density, viscosity and boiling point
Refractive index and surface tension
Both (A) and (B)
None of these
Entropy
Internal energy
Enthalpy
Gibbs free energy
Tds = dE - dW = 0
dE - dW - Tds = 0
Tds - dE + dW < 0
Tds - dT + dW < 0
Positive
Negative
Zero
Infinity
Pressure
Temperature
Both (A) & (B)
Neither (A) nor (B)
A homogeneous solution (say of phenol water) is formed
Mutual solubility of the two liquids shows a decreasing trend
Two liquids are completely separated into two layers
None of these
Specific heat
Latent heat of vaporisation
Viscosity
Specific vapor volume
More
Less
Same
Data insufficient to predict
Freon
Liquid sulphur dioxide
Methyl chloride
Ammonia
Departure from ideal solution behaviour
Departure of gas phase from ideal gas law
Vapour pressure of liquid
None of these
Chemical potential
Activity
Fugacity
Activity co-efficient