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The Effect of Temperature on Mutual Solubility

We have considered so far the effect of nonideality on the mixing of the two liquids, at a specified temperature of 300 K, by varying the value of A in Eq. 12.10.1. We examine next the effect that temperature has on the mixing of the two liquids. To this purpose we keep, for simplicity, A independent of temperature and equd to 4 kJ/mol, a value that leads to complete miscibility at 300 K. [Pg.427]

At this temperature the two liquid phases merge into one, i.e. their properties become identical, and it is referred to as the critical solution (or consolute) temperature. [Pg.428]

The maximum temperature at which phase separation is possible independent of composition, occurs at Xj = 2 = 0.5  [Pg.428]

We conclude that at temperatures higher than 240.5 K a single liquid is the equilibrium state at lower ones, two liquid phases at equilibrium are present. This is demonstrated in the following Example. [Pg.428]

Equations 12.10.5 through 12.10.12 are based on the use of the two-suffix (one-parameter) Margules expression for the excess Gibbs free energy (Eq. 12.10.1). It is a very simple model which, even with a temperature dependent A, is applicable to a very limited number of systems where is a symmetric function of a i, mainly hydrocarbons of similar size. [Pg.429]


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