Expansion valve
Condenser
Refrigerator
Compressor
D. Compressor
Vapor pressure
Specific Gibbs free energy
Specific entropy
All (A), (B) and (C)
Enthalpy
Internal energy
Either (A) or (B)
Neither (A) nor (B)
Logarithmic
Arithmetic
Geometric
Harmonic
its internal energy (U) decreases and its entropy (S) increases
U and S both decreases
U decreases but S is constant
U is constant but S decreases
0
1
< 1
> 1
In which there is a temperature drop
Which is exemplified by a non-steady flow expansion
Which can be performed in a pipe with a constriction
In which there is an increase in temperature
Decreases
Increases
Remain same
May increase or decrease; depends on the nature of the gas
Free expansion of a gas
Compression of air in a compressor
Expansion of steam in a turbine
All (A), (B) & (C)
Heat
Momentum
Energy
Work
Volume
Temperature
Pressure
None of these
Critical
Triple
Freezing
Boiling
Binary solutions
Ternary solutions
Azeotropic mixture only
None of these
Isothermal
Irreversible
Adiabatic
Reversible
Pressure
Temperature
Both (A) & (B)
Neither (A) nor (B)
Decreases
Increases
Remains constant
Decreases logarithmically
Positive
Negative
Zero
Infinity
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
Enthalpy
Volume
Both 'a' & 'b'
Neither 'a' nor 'b'
μ = (∂P/∂T)H
μ = (∂T/∂P)H
μ = (∂E/∂T)H
μ = (∂E/∂P)H
Decrease in temperature
Increase in temperature
No change in temperature
Change in temperature which is a function of composition
Specific volume
Temperature
Mass
Pressure
5 & 3
3.987 & 1.987
1.987 & 0.66
0.66 & 1.987
Less pronounced
More pronounced
Equal
Data insufficient, can't be predicted
Departure from ideal solution behaviour
Departure of gas phase from ideal gas law
Vapour pressure of liquid
None of these
RT d ln P
RT d ln f
R d ln f
None of these
T2/(T1 - T2)
T1/(T1 - T2)
(T1 - T2)/T1
(T1 - T2)/T2
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
Specific heat at constant pressure (Cp)
Specific heat at constant volume (Cv)
Joule-Thompson co-efficient
None of these
Property of the system
Path function
Point function
State description of a system
Water
Ammonia
Freon
Brine