Theoretical and Experimental Evaluation of a Distillation–Pervaporation in a Single Unit Column for the Separation of an Azeotropic Mixture-Reference-Cited by-同舟云学术

Theoretical and Experimental Evaluation of a Distillation–Pervaporation in a Single Unit Column for the Separation of an Azeotropic Mixture

Published:2020-10-16 Issue:43 Volume:59 Page:19426-19437
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

León Juan A.¹,Fontalvo Javier¹^ORCID

Affiliation:

1. Laboratory of Processes Intensification and Hybrid Systems − LIPSH, Department of Chemical Engineering, Universidad Nacional de Colombia−sede Manizales, P.O. Box 127, Caldas 170003, Colombia

Funder

Departamento Administrativo de Ciencia, Tecnolog?a e Innovaci?n

Universidad Nacional de Colombia, Sede Manizales

Publisher

American Chemical Society (ACS)

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/acs.iecr.0c03885

Reference26 articles.

1. Design and control of pressure-swing distillation for separating ternary systems with three binary minimum azeotropes

2. Review of extractive distillation. Process design, operation, optimization and control

3. Vapour–liquid equilibrium and extractive distillation for separation of azeotrope isopropyl alcohol and diisopropyl ether

4. Enhanced separation of maximum boiling azeotropic mixtures with extractive heterogeneous-azeotropic distillation

5. Comparison of pressure-swing distillation with or without crossing curved-boundary for separating a multiazeotropic ternary mixture

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