Solubility and Liquid–Liquid Equilibria for the Isopropyl Acetate + Isopropanol + Acetic Acid + Water Quaternary System at 313.15 K and 101.3 kPa
Author:
Affiliation:
1. Institute of Chemical Engineering, East China University of Science and Technology, Shanghai 200237, China
Publisher
American Chemical Society (ACS)
Subject
General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/acs.jced.9b00595
Reference23 articles.
1. Optimization and control of a reactive and extractive distillation process for the synthesis of isopropyl acetate
2. A Systematic Method for the Development of Operating Policies for Two-Step Processes with Semibatch Reactive Distillation
3. A thermally coupled reactive distillation process to intensify the synthesis of isopropyl acetate
4. Isothermal Vapor−Liquid Equilibrium in the Quaternary Water + 2-Propanol + Acetic Acid + Isopropyl Acetate System with Chemical Reaction
5. Phase and reaction equilibria of the acetic acid-isopropanol-isopropyl acetate-water system at 760 mmHg
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1. Liquid–Liquid Phase Equilibrium for the Ternary System (Water–Ethanol–Ethyl Caprate): Experimental and Modeling;Journal of Chemical & Engineering Data;2024-05-30
2. Vapor–Liquid and Chemical Equilibrium for Esterification of Acetic Acid + Isopropanol with [HSO3-bmim][HSO4] at 101.33 kPa;Journal of Solution Chemistry;2023-08-06
3. Solvent extraction of acetic acid from aqueous solutions: A review;Separation Science and Technology;2023-07-03
4. Vapor-Liquid and Chemical Equilibrium for Esterification of Acetic Acid + Isopropanol with [HSO3 -bmim][HSO4 ] at 101.33 kPa;2023-02-22
5. Modeling and optimizing the synthesis of isopropyl acetate over niobium pentoxide using experimental design methodology coupled with artificial neural network;Chemical Engineering Communications;2023-02-07
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