Ideal Solution
7. Ideal Solution
a. Volume
A liquid mixture in which all of the components are miscible at the molecular level is called an ideal solution, provided the following condition is satisfied, i.e.,
(59) In an ideal solution, the forces between the unlike molecules are assumed to be the same as
ˆv id
id
k = v k , and v = Σ k X k v k = Σ k X k v k .
those between like molecules.
b. Internal Energy and Enthalpy In ideal mixture of liquids or real gases,
h id = Σ
k X k h k , and
id id
u id = h – P v = Σ
k X k ( h k –P v k ).
c. Gibbs Function At a specified temperature, the change in the Gibbs free energy of a pure component (i.e. when it is alone at T and P) is given as (Chapter 7)
d g k = v k (T, P) dP, i.e., (a) If the composition and temperature in a mixture are held fixed and the pres-
sure is altered then applying Eq.(31) for k in a mixture
d ˆg k = ˆv k (T, P, X k ) dP (62a) Then from Eqs. (a) and (62a) d( ˆg k – g k )=( ˆv k (T, P, X k )– v k (T, P))dP.
(62b) If a mixture of fixed composition is subjected to an incremental pressure dP, and the pure
component is also subjected to the same pressure increment, this expression provides the dif- ference between two Gibbs function ˆg k and g k due to difference in ˆv k and v k . For example,
H 2 O in the solution is compressed from 200 to 250 kPa, with ˆv HO 2 = 0.015 m 3 kmole –1 , dg ˆ HO
and d g H2O = 0.9 kJkmole . Integrating
2 = 0.75 kJ kmole -1 . On the other hand,
v H2O = 0.018 m kmole
3 -1
ˆg k – g k = ∫( ˆv k – v k )dP + f(T, X k ). In an ideal solution at any temperature and pressure, ˆv k = v k and hence
– g k = f(T, X k ). As P →0 at a specified temperature and composition the same relation should hold good.
ˆg id
Hence id ˆg
and g k approach their corresponding values in an ideal gas. Therefore, f(T, X k )= R T ln X k . consequently, in an ideal solution ˆg id
= g k (T, P) + R T ln X k or ˆg k id - g k (T, P) = R T ln X k . (62c)
d. Entropy Since,
= ˆh k –T ˆs k (T, P, X k )= ˆh k –T s k (T, P) + R T ln X k i.e., then ˆs k (T, P, X k )= s k (T, P)– R ln X k .
ˆg id
(63) The entropy of the ideal mixture is S id (T, P, N) =
(T, P, X )N , and s Σ id k s k k k =S id /N = Σ k s k (T, P, X k )X k . (64)
g. Example 8 Lake water at 25ºC and 1 bar absorbs air from the atmosphere. If the air mole fraction in the liquid is 0.001, what is the entropy of H 2 O in the lake water?
Solution Air consists of O 2 and N 2 molecules that have weak attractive forces between them- selves in the atmosphere. However once these molecules enter liquid water, they are surrounded by H 2 O molecules which exert strong attractive forces and hold the gas molecules in the liquid phase. Thereby, small amounts of air become dissolved in liq- uid water.
ˆs HO 2 (25ºC, 1 bar, 0.999) = s HO 2 (25ºC, 1 bar) – R ln X HO 2 .
Pure water exists at 25ºC and 1 bar as a compressed liquid. We will assume that the liquid is incompressible and that s HO 2 (25ºC, P sat = 0.032 bar) = s HO 2 (25ºC, 1 bar) =
6.621 kJ kmole –1 K . Therefore, ˆs –1
HO 2 (25ºC, 1 bar, 0.999) = 6.621 – 8.314 × ln 0.999 = 6.629 kJ kmole .
Parts
» COMPUTATIONAL MECHANICS and APPLIED ANALYSIS
» Explicit and Implicit Functions and Total Differentiation
» Exact (Perfect) and Inexact (Imperfect) Differentials
» Intermolecular Forces and Potential Energy
» Internal Energy, Temperature, Collision Number and Mean Free Path
» Vector or Cross Product r The area A due to a vector product
» First Law for a Closed System
» First Law For an Open System
» STATEMENTS OF THE SECOND LAW
» Cyclical Integral for a Reversible Heat Engine
» Irreversibility and Entropy of an Isolated System
» Degradation and Quality of Energy
» SINGLE–COMPONENT INCOMPRESSIBLE FLUIDS
» Evaluation of Entropy for a Control Volume
» Internally Reversible Work for an Open System
» MAXIMUM ENTROPY AND MINIMUM ENERGY
» Generalized Derivation for a Single Phase
» LaGrange Multiplier Method for Equilibrium
» Absolute and Relative Availability Under Interactions with Ambient
» Irreversibility or Lost Work
» Applications of the Availability Balance Equation
» Closed System (Non–Flow Systems)
» Heat Pumps and Refrigerators
» Work Producing and Consumption Devices
» Graphical Illustration of Lost, Isentropic, and Optimum Work
» Flow Processes or Heat Exchangers
» CLASSICAL RATIONALE FOR POSTULATORY APPROACH
» Generalized Legendre Transform
» Van der Waals (VW) Equation of State
» Other Two–Parameter Equations of State
» Compressibility Charts (Principle of Corresponding States)
» Boyle Temperature and Boyle Curves
» Three Parameter Equations of State
» Empirical Equations Of State
» State Equations for Liquids/Solids
» Internal Energy (du) Relation
» EXPERIMENTS TO MEASURE (u O – u)
» Vapor Pressure and the Clapeyron Equation
» Saturation Relations with Surface Tension Effects
» Temperature Change During Throttling
» Throttling in Closed Systems
» Procedure for Determining Thermodynamic Properties
» Euler and Gibbs–Duhem Equations
» Relationship Between Molal and Pure Properties
» Relations between Partial Molal and Pure Properties
» Mixing Rules for Equations of State
» Partial Molal Properties Using Mixture State Equations
» Ideal Solution and Raoult’s Law
» Completely Miscible Mixtures
» DEVIATIONS FROM RAOULT’S LAW
» Mathematical Criterion for Stability
» APPLICATION TO BOILING AND CONDENSATION
» Physical Processes and Stability
» Constant Temperature and Volume
» Equivalence Ratio, Stoichiometric Ratio
» Entropy, Gibbs Function, and Gibbs Function of Formation
» Entropy Generated During an Adiabatic Chemical Reaction
» MASS CONSERVATION AND MOLE BALANCE EQUATIONS
» Evaluation of Properties During an Irreversible Chemical Reaction
» Criteria in Terms of Chemical Force Potential
» Generalized Relation for the Chemical Potential
» Nonideal Mixtures and Solutions
» Gas, Liquid and Solid Mixtures
» Availability Balance Equation
Show more