Identificador persistente para citar o vincular este elemento: http://hdl.handle.net/10553/132052
Título: Contribution to a sustainable process for the production of isopropanol through the proper management of thermodynamic data
Autores/as: Domínguez Déniz, Leandro 
Ortega, Juan 
Fernández, Luis 
Maarouf Bassaidi, Mustapha 
Lorenzo Pérez, Beatriz 
Clasificación UNESCO: 3303 ingeniería y tecnología químicas
Palabras clave: Liquid-liquid equilibrium
Water
Iso-propanol
Ethyl pentanoate
Azeotropic mixture, et al.
Fecha de publicación: 2023
Proyectos: DISEÑO SOSTENIBLE Y ECO-EFICIENTE DE PROCESOS DE PRODUCCIÓN DE CARBONATO DE GLICEROL PARA REVALORIZAR EL GLICEROL RESIDUAL DE LA OBTENCIÓN DEL BIODIESEL
Publicación seriada: Trends in Chemical Engineering 
Resumen: Iso-propanol is a compound of interest widely used in various sectors, both industrially and in scientific research. However, its purification has drawbacks as it forms an azeotrope with water, making separation difficult. In this work the separation of the azeotrope water+iso-propanol by liquid-liquid extraction using ethyl pentanoate as entrainer is studied. Following a sequence of tasks such as experimentation↔modeling↔simulation, this work presents new LLE information of the binary and ternary systems involved. The feasibility of the process is analyzed in a commercial simulator using a model generated from experimental information, and VLE data estimated with UNIFAC. The ternary system produces a type I liquid-liquid equilibrium, the correlation of which is performed with acceptable results. The simulation results show that the liquid-liquid extraction, properly integrated with a fractional distillation, allows the recovery of almost 100% of iso-propanol with a purity close to 81% (w/w).
URI: http://hdl.handle.net/10553/132052
ISSN: 0972-4478
Fuente: Trends in Chemical Engineering [ISSN 0972-4478], v. 21, p. 13-25, (2023)
Colección:Artículos
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