Isothermal
Irreversible
Adiabatic
Reversible
B. Irreversible
Are more or less constant (vary from 0.2 to 0.3)
Vary as square of the absolute temperature
Vary as square of the absolute pressure
None of these
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
μ = (∂P/∂T)H
μ = (∂T/∂P)H
μ = (∂E/∂T)H
μ = (∂E/∂P)H
Expansion in an engine
Following a constant pressure cycle
Throttling
None of these
∞
1
0
-ve
Oxygen
Nitrogen
Air
Hydrogen
F = A + PV
F = E + A
F = A - TS
F = A + TS
Amount of energy transferred
Direction of energy transfer
Irreversible processes only
Non-cyclic processes only
Activity co-efficient is dimensionless.
In case of an ideal gas, the fugacity is equal to its pressure.
In a mixture of ideal gases, the fugacity of a component is equal to the partial pressure of the component.
The fugacity co-efficient is zero for an ideal gas
Tds = dE - dW = 0
dE - dW - Tds = 0
Tds - dE + dW < 0
Tds - dT + dW < 0
Increases, for an exothermic reaction
Decreases, for an exothermic reaction
Increases, for an endothermic reaction
None of these
3
2
1
0
0
1
2
3
Pressure and temperature
Reduced pressure and reduced temperature
Critical pressure and critical temperature
None of these
Fusion
Vaporisation
Transition
None of these
0.5
3.5
4.5
8.5
Entropy
Gibbs energy
Internal energy
Enthalpy
ΔF = ΔH + T [∂(ΔF)/∂T]P
ΔF = ΔH - TΔT
d(E - TS) T, V < 0
dP/dT = ΔHvap/T.ΔVvap
Decreases
Decreases exponentially
Increases
Remain constant
0
1
2
3
Solid-vapor
Solid-liquid
Liquid-vapor
All (A), (B) and (C)
Low pressure and high temperature
Low pressure and low temperature
Low temperature and high pressure
High temperature and high pressure
Two
One
Zero
Three
0°C and 750 mm Hg
15°C and 750 mm Hg
0°C and 1 kgf/cm2
15°C and 1 kgf/cm2
Increases
Decreases
Remain same
Decreases linearly
Is the analog of linear frictionless motion in machines
Is an idealised visualisation of behaviour of a system
Yields the maximum amount of work
Yields an amount of work less than that of a reversible process
Adiabatic
Isothermal
Isometric
None of these
Cp/Cv
Cp/(CP-R)
1 + (R/CV)
All (A), (B) and (C)
dQ = dE + dW
dQ = dE - dW
dE = dQ + dW
dW = dQ + dE
High thermal conductivity
Low freezing point
Large latent heat of vaporisation
High viscosity