Phase behaviour of ethanol plus water plus ethyl acetate at 101.3 kPa

被引:4
作者
Iglesias, Miguel [1 ]
Gonzalez-Olmos, Rafael [1 ]
Manuel Goenaga, Jose [2 ]
Maria Resa, Jose [2 ]
机构
[1] Univ Santiago Compostela, Sch Engn, Dept Chem Engn, PF&PT Res Team, E-15782 Santiago De Compostela, Spain
[2] Univ Basque Country, Dept Ingn Quim, Vitoria 01006, Spain
关键词
azeotrope; ethanol; water; ethyl acetate; phase equilibria; prediction; thermodynamic topological analysis; TERNARY-SYSTEMS; EQUILIBRIA; THERMODYNAMICS; TEMPERATURE; PREDICTION; COMPONENTS; MIXTURES; WINE;
D O I
10.1080/00319100903096539
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Must distillation processes simulation is a challenging task, due to the lack of thermodynamic interaction parameters and accurate studies of phase equilibria. The presence of polar substances, those different from ethanol and water, and their low concentrations make it very difficult to model industrial distillation. Several of the congeners are essential enological components of the organoleptic matrix. In this work, we are concerned with the study of phase behaviour of ethanol + water + ethyl acetate at 101.3 kPa, this being the third compound, the legal congener of the highest composition in common alcoholic distillation. The experimental results showed partial miscibility and four azeotropes into a complex medium. Group contribution models yield poor results. Disposable literature was compared and commented upon. The lack of experimental data in multicomponent alcoholic distillation mixtures and the low reliability of the group contribution methods suggest a prudent application to process simulation.
引用
收藏
页码:461 / 476
页数:16
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