What is the difference between UNIQUAC and UNIFAC models?

Theories of Solutions : Excess functions (and consequently activity coefficients) can be obtained from equations of state. However, this approach has limited practical applicability.


Lattice Models :

Liquid is considered to be a quasicrystalline state with molecules arranged in a

regular array. Mixing two different liquid to obtain a solution results in the

entropy of mixing (as lattice structure is altered) and enthalpy of mixing (due to

intermolecular forces). The potential energy of the system is obtained by pairwise

addition of all molecular pairs considering only the nearest neighbors. An

expression for Helmholtz energy can be derived in terms of the interchange

energy (w) which arises when a molecule of one component in the lattice is

replaced by the molecule of the second component. The interchange energy is

dependent upon the difference in the potential energies of pairs 1-2, 1-1 and 2-2

(for a binary mixture of 1 and 2). For a regular solution the excess Gibbs energy is

equal to excess Helmholtz energy, leading to a method for calculation of activity

coefficients. The interchange energy can be calculated from potential functions

and molecular properties, primarily for mixtures of nonpolar molecules similar in

size. This approach is not very useful for mixtures having additional complexities.


Non-random Mixtures:

A solution is essentially non-random in nature as in most cases intermolecular

forces for different compounds are not identical. So in a binary mixture of 1 and

2, molecules of 1 either prefer 2 or 1 as immediate neighbors. The solution has

certain order to it resulting in sE < 0. A quasichemical theory for such solutions

can be developed by writing an equilibrium constant expression for the formation

of complex 1–2 from molecules of 1 and 2. The equilibrium constant is related to

the interchange energy w, leading to expressions for excess Helmholtz energy,

excess entropy and excess Gibbs energy.


Two-Liquid Theory:

Since the solutions are essentially non-random, they can be thought of as

comprised of 2 (or more) hypothetical fluids depending upon the nature of

interaction between the solution components. The thermodynamic properties of

the solution are then mole fraction weighted averages of the properties of the

hypothetical fluids. Area fractions and volume fractions can be defined for each

hypothetical fluid, and expressions developed for the excess properties of the

solution. The UNIQUAC equation, developed on the basis of two- liquid theory is

quite successful, however, it may over-correct for non-randomness of the

solution.


Group Contribution Methods

Activity coefficients can be calculated for various mixtures by considering

individual molecules to be comprised of different functional groups. The number

of distinct functional groups (methyl, methylene, hydroxyl, etc.) is relatively

small compared to the number of distinct compounds. The interaction between

various compounds is obtained by contributions of the functional group

interaction for the compounds. ASOG (analytical solution of groups) and

UNIFAC (universal functional activity coefficient) are two group contribution

methods that are quite useful. Group contribution methods are very rapid,

however, they may not necessarily be accurate. The results of the group

contribution methods need to be compared with experimental data for validation.


Chemical Theory of Non- ideality of Liquid Solutions:

The non- ideality of the solutions is due to formation of new species by the

reactions of the components. These reactions may be associations of a single

component (dimmer, trimer, polymer formation) or solvation (interactions of two

or more components, e.g. complexation). These species are at chemical

equilibrium with each other and form ideal solutions. Therefore, the behavior of

the solution can be described if the “true” composition of the solution is determined.

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