Compressibility
Work done under adiabatic condition
Work done under isothermal condition
Co-efficient of thermal expansion
C. Work done under isothermal condition
Isothermal compression
Isothermal expansion
Adiabatic expansion
Adiabatic compression
Water
Air
Evaporative
Gas
0
< 0
> 0
A function of pressure
Work done under adiabatic condition
Co-efficient of thermal expansion
Compressibility
None of these
Critical temperature
Melting point
Freezing point
Both (B) and (C)
Vapor pressure
Partial pressure
Chemical potential
None of these
1
< 1
> 1
Either (B) or (C), depends on the nature of the gas
Isothermally
Isobarically
Adiabatically
None of these
Straight line
Sine curve
Parabola
Hyperbola
RT d ln P
RT d ln f
R d ln f
None of these
2
0
3
1
Temperature
Pressure
Volume
None of these
Critical
Boyle
Inversion
Reduced
dQ = dE + dW
dQ = dE - dW
dE = dQ + dW
dW = dQ + dE
Minimum
Zero
Maximum
None of these
Zeroth
First
Second
Third
Minimum number of degree of freedom of a system is zero
Degree of freedom of a system containing a gaseous mixture of helium, carbon dioxide and hydrogen is 4
For a two phase system in equilibrium made up of four non-reacting chemical species, the number of degrees of freedom is 4
Enthalpy and internal energy change is zero during phase change processes like melting, vaporisation and sublimation
Enthalpy
Entropy
Pressure
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
Evaporation
Liquid extraction
Drying
Distillation
Specific volume
Temperature
Mass
Pressure
Turbine
Heat engine
Reversed heat engine
None of these
Internal energy
Enthalpy
Gibbs free energy
Helmholtz free energy
Any
A perfect
An easily liquefiable
A real
Equation of state
Gibbs Duhem equation
Ideal gas equation
None of these
Two
One
Zero
Three
PV
2PV
PV/2
0
Isothermal
Isentropic
Isobaric
Adiabatic
Increased COP
Same COP
Decreased COP
Increased or decreased COP; depending upon the type of refrigerant
Moisture free ice
Solid helium
Solid carbon dioxide
None of these