Vapor–Liquid Equilibrium Experiment and Thermodynamic Model Correlation for Ethanol + Isopropyl Acetate with Ionic Liquid at 101.3 kPa
Author:
Affiliation:
1. State Key Laboratory of Chemical Resource Engineering, Beijing University of Chemical Technology, Box 266, Beijing 100029, China
Funder
National Natural Science Foundation of China
Publisher
American Chemical Society (ACS)
Subject
General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/acs.jced.2c00778
Reference27 articles.
1. Current status and future prospective of bio-ethanol industry in China
2. A reactive distillation process with a sidedraw stream to enhance the production of isopropyl acetate
3. Homogeneous azeotropic distillation: Comparing entrainers
4. Investigation of a Batch Azeotropic Distillation for the Separation of Acetic Acid‐Water Mixtures
5. Review of extractive distillation. Process design, operation, optimization and control
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1. Vapor–Liquid Equilibrium for Ethyl Acetate + Acetonitrile with Acetate-Based Ionic Liquids as Entrainers at 101.3 kPa and Analysis of the Separation Mechanism;Journal of Chemical & Engineering Data;2024-03-08
2. Vapor–Liquid Equilibrium for Acetonitrile + Ethanol with Imidazole-Based Ionic Liquids as Entrainers at 101.3 kPa;Journal of Chemical & Engineering Data;2024-03-06
3. Isobaric Vapor-Liquid Equilibrium for Ethyl Acetate + Acetonitrile with Ionic Liquid [Bmim][Ac] as an Entrainer and Analysis of Separation Mechanism;2023
4. Vapor-Liquid Equilibrium for Acetonitrile + Ethanol with Ionic Liquid [Bmim][Dep] as an Entrainer at 101.3 Kpa and Analysis of Separation Mechanism;2023
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