Unity
Zero
That of the heat of reaction
Infinity
B. Zero
Endothermic
Exothermic
Isothermal
Adiabatic
Decreases
Increases
Remain same
May increase or decrease; depends on the nature of the gas
Equilibrium
Adiabatic
Steady
Unsteady
Polar
Non-polar
Both (A) & (B)
Neither (A) nor (B)
Two temperatures only
Pressure of working fluid
Mass of the working fluid
Mass and pressure both of the working fluid
Melting point of ice
Melting point of wax
Boiling point of liquids
None of these
Entropy
Temperature
Enthalpy
Pressure
1.987 cal/gm mole °K
1.987 BTU/lb. mole °R
Both (A) and (B)
Neither (A) nor (B)
Independent of pressure
Independent of temperature
Zero at absolute zero temperature for a perfect crystalline substance
All (A), (B) & (C)
Equation of state
Gibbs Duhem equation
Ideal gas equation
None of these
6738.9
6753.5
7058.3
9000
Heating takes place
Cooling takes place
Pressure is constant
Temperature is constant
PV
2PV
PV/2
0
Δ H = 0 and ΔS = 0
Δ H ≠ 0 and ΔS = 0
Δ H ≠ 0 and ΔS ≠ 0
Δ H = 0 and ΔS ≠ 0
High temperature
Low pressure
Low temperature only
Both low temperature and high pressure
Carnot
Air
Absorption
vapour-ejection
Superheated vapour
Partially condensed vapour with quality of 0.9
Saturated vapour
Partially condensed vapour with quality of 0.1
Adiabatic
Reversible
Isothermal
None of these
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
State functions
Path functions
Intensive properties
Extensive properties
0
∞
50
100
Heat capacity of a crystalline solid is zero at absolute zero temperature
Heat transfer from low temperature to high temperature source is not possible without external work
Gases having same reduced properties behaves similarly
None of these
Specific volume
Work
Pressure
Temperature
Gibbs-Duhem equation
Gibbs-Helmholtz equation
Third law of thermodynamics
Joule-Thomson effect
Critical temperature
Melting point
Freezing point
Both (B) and (C)
RT ln K
-RT ln K
-R ln K
T ln K
(∂T/∂V)S = (∂p/∂S)V
(∂T/∂P)S = (∂V/∂S)P
(∂P/∂T)V = (∂S/∂V)T
(∂V/∂T)P = -(∂S/∂P)T
Specific heat at constant pressure (Cp)
Specific heat at constant volume (Cv)
Joule-Thompson co-efficient
None of these
Isobaric
Adiabatic
Isenthalpic
Both (B) & (C)
Two isothermal and two isentropic
Two isobaric and two isothermal
Two isochoric and two isobaric
Two isothermals and two isochoric