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