Phase equilibria of the water + 1-butanol + toluene ternary system at 101.3 kPa


Autoria(s): Gomis Yagües, Vicente; Font, Alicia; Saquete Ferrándiz, María Dolores; García Cano, Jorge
Contribuinte(s)

Universidad de Alicante. Departamento de Ingeniería Química

Universidad de Alicante. Instituto Universitario de Ingeniería de los Procesos Químicos

Equilibrio entre Fases

Data(s)

07/11/2014

07/11/2014

15/01/2015

Resumo

Isobaric vapour–liquid and vapour–liquid–liquid equilibrium data for the water + 1-butanol + toluene ternary system were measured at 101.3 kPa with a modified VLE 602 Fischer apparatus. In addition, the liquid–liquid equilibrium data at 313.15 K were measured and compared with data from other authors at different temperatures. The system exhibits a ternary heterogeneous azeotrope whose temperature and composition have been determined by interpolation. The thermodynamic consistency of the experimental vapour–liquid and vapour–liquid–liquid data was checked by means of the Wisniak’s Li/Wi consistency test. Moreover, the vapour–liquid and the liquid–liquid equilibrium correlation for the ternary system with NRTL and UNIQUAC models, together with the prediction made with the UNIFAC model, were studied and discussed.

The authors thank the DGICYT of Spain for the financial support of project CTQ2009-13770.

Identificador

Fluid Phase Equilibria. 2015, 385: 29-36. doi:10.1016/j.fluid.2014.10.038

0378-3812 (Print)

1879-0224 (Online)

http://hdl.handle.net/10045/42119

10.1016/j.fluid.2014.10.038

Idioma(s)

eng

Publicador

Elsevier

Relação

http://dx.doi.org/10.1016/j.fluid.2014.10.038

Direitos

info:eu-repo/semantics/openAccess

Palavras-Chave #Water #1-Butanol #Toluene #Liquid–liquid equilibrium #Vapour–liquid–liquid equilibrium #Ingeniería Química
Tipo

info:eu-repo/semantics/article