Thermodynamics of liquid-liquid equilibria including the critical region
✍ Scribed by Juan José De Pablo; John M. Prausnitz
- Publisher
- American Institute of Chemical Engineers
- Year
- 1988
- Tongue
- English
- Weight
- 1021 KB
- Volume
- 34
- Category
- Article
- ISSN
- 0001-1541
No coin nor oath required. For personal study only.
✦ Synopsis
To obtain good representation in the liquid-liquid critical region, a semitheoretical correction is added to a conventional expression (e.g., van Laar or NRTL) for the excess Gibbs energy of a binary or ternary system along the coexistence curve. This correction is an exponential function of a suitable distance from the critical point; it is significant in the critical region but not elsewhere. In the correction function, the preexponential factor is determined from stability considerations. In the exponential argument, two parameters are determined from theoretical power laws. While the coordinates of the critical point must be known (or estimated), no phase-equilibrium data in the critical region are required to determine parameters. The correction presented here provides an excellent approximation for phase equilibria along the coexistence curve close t o and remote from critical conditions. Further, the correction facilitates simultaneous representation of isothermal vaporliquid and liquid-liquid equilibria including the liquid-liquid critical region.
📜 SIMILAR VOLUMES
An exact graphical method for the evaluation of vapour-liquid equilibrium data in a binary mixture from boiling point composition data is described. The variation of the activity coefficients with composition is obtained by successive application of the exact Duhem equation to a graph relating ln yr
The coexistence curves for x CHCOOC H q 1 y x CH CH CH have been 2 5 2 3 2 5 3 determined within about 10 K from the critical temperature by measurements of the refractive Ž . index. The critical amplitude B, and the critical exponent  have been deduced from T, n , Ž . Ž . T, x and T, curves where
A?Mract-Saturated state thermodynaimc propeNes of ref~rants are prcdrctcd from cnt~cal coordmates and normaI bodmg pomts by usmg Soave's equabon of state Bmary vapor-hquni cqtuhbna are correlated by determmmg mteraction parameters for the followmg SEX systems CC12FJCH3CHF2. CCIJ;JCHCIF~, CHF&X3F3, C