Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Author:
Affiliation:
1. Departamento de Ingeniería Química Básica, Universidad del Zulia, 4011, Maracaibo, Venezuela
2. Departamento de Ingeniería Química, Escuela Técnica Superior de Ingeniería, Universitat de València, 46100 Burjassot, Valencia, Spain
Publisher
American Chemical Society (ACS)
Subject
General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/je200784y
Reference19 articles.
1. Isobaric Vapor−Liquid Equilibria for Binary and Ternary Mixtures with Cyclohexane, Cyclohexene, and 2-Methoxyethanol at 100 kPa
2. Isobaric vapor–liquid equilibria for binary and ternary mixtures with cyclohexane, cyclohexene, and morpholine at 100kPa
3. Isobaric Vapor−Liquid Equilibria for Binary and Ternary Mixtures with Cyclohexane, Cyclohexene, and Methyl Isobutyl Ketone at 100 kPa
4. Isobaric vapor–liquid equilibrium for binary mixtures of 1-hexene+n-hexane and cyclohexane+cyclohexene at 30, 60 and 101.3kPa
5. Isobaric Vapor−Liquid Equilibria of Diethyl Carbonate with Four Alkanes at 101.3 kPa
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2. Isothermal Vapor–Liquid Equilibrium (P–x–y) Measurements and Modeling of n-Hexane + Pentan-2-one/4-Methylpentan-2-one;Journal of Chemical & Engineering Data;2020-10-06
3. A review of extractive distillation from an azeotropic phenomenon for dynamic control;Chinese Journal of Chemical Engineering;2019-07
4. Isobaric Vapor–Liquid Equilibria of Binary Mixtures of Diethyl Carbonate with Methyl Acetate, n-Propyl Acetate, or Amyl Acetate at 100.17 kPa;Journal of Chemical & Engineering Data;2019-05-29
5. Energy-efficient heterogeneous extractive distillation system for the separation of close-boiling cyclohexane/cyclohexene mixture;Journal of the Taiwan Institute of Chemical Engineers;2018-06
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