Molar concentration
Quantity (i.e. number of moles)
Both (A) and (B)
Neither (A) nor (B)
C. Both (A) and (B)
The available energy in an isolated system for all irreversible (real) processes decreases
The efficiency of a Carnot engine increases, if the sink temperature is decreased
The reversible work for compression in non-flow process under isothermal condition is the change in Helmholtz free energy
All (A), (B) and (C)
Cp/Cv
Cp/(CP-R)
1 + (R/CV)
All (A), (B) and (C)
Temperature
Pressure
Volume
Entropy
The expansion of a gas in vacuum is an irreversible process
An isometric process is a constant pressure process
Entropy change for a reversible adiabatic process is zero
Free energy change for a spontaneous process is negative
J/s
J.S
J/kmol
kmol/J
Less than
Equal to
More than
Either (B) or (C); depends on the type of alloy
∞
0
< 0
> 0
Increases with increase in pressure
Decreases with increase in temperature
Is independent of temperature
None of these
Pressure
Composition
Temperature
All (A), (B) and (C)
High thermal conductivity
Low freezing point
Large latent heat of vaporisation
High viscosity
Single phase fluid of varying composition
Single phase fluid of constant composition
Open as well as closed systems
Both (B) and (C)
Only ΔE = 0
Only ΔH =0
ΔE = ΔH = 0
dQ = dE
0
1
2
3
Increases
Decreases
Remains unchanged
First decreases and then increases
x
x + 1
x + 2
x + 3
∞
-ve
0
+ve
Amount of energy transferred
Direction of energy transfer
Irreversible processes only
Non-cyclic processes only
2
0
1
3
The chemical potential of a pure substance depends upon the temperature and pressure
The chemical potential of a component in a system is directly proportional to the escaping tendency of that component
The chemical potential of ith species (μi) in an ideal gas mixture approaches zero as the pressure or mole fraction (xi) tends to be zero at constant temperature
The chemical potential of species 'i' in the mixture (μi) is mathematically represented as,μi = ∂(nG)/∂ni]T,P,nj where, n, ni and nj respectively denote the total number of moles, moles of ith species and all mole numbers except ith species. 'G' is Gibbs molar free energy
Volume
Pressure
Temperature
All (A), (B) and (C)
Use of only one graph for all gases
Covering of wide range
Easier plotting
More accurate plotting
Superheated
Desuperheated
Non-condensable
None of these
+ve
0
-ve
∞
Entropy
Temperature
Enthalpy
Pressure
d ln p/dt = Hvap/RT2
d ln p/dt = RT2/Hvap
dp/dt = RT2/Hvap
dp/dt = Hvap/RT2
Entropy
Gibbs free energy
Internal energy
All (A), (B) & (C)
Low temperature
High pressure
Both (A) and (B)
Neither (A) nor (B)
Steam engine
Carnot engine
Diesel engine
Otto engine
Volume
Mass
Critical temperature
None of these
T2/(T1 - T2)
T1/(T1 - T2)
(T1 - T2)/T1
(T1 - T2)/T2