Isobaric Vapor–Liquid Equilibrium of Ethyl Acetate + 1-Hexanol, Methanol + 1-Hexanol, and n-Heptane + Cyclohexanol Binary System at 101.3 kPa
Author:
Affiliation:
1. College of Chemical Engineering, Qingdao University of Science and Technology, Qingdao 266042, 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.3c00245
Reference41 articles.
1. Enhanced separation of benzene and cyclohexane by homogeneous extractive distillation using ionic liquids as entrainers
2. A review of extractive distillation from an azeotropic phenomenon for dynamic control
3. Energy, economic and environmental evaluations for the separation of ethyl acetate/ethanol/water mixture via distillation and pervaporation unit
4. Homogeneous catalysts for CO2 hydrogenation to methanol and methanol dehydrogenation to hydrogen generation
5. Three-Stage Conversion of Chemically Inert n-Heptane to α-Hydrazino Aldehyde Based on Bioelectrocatalytic C–H Bond Oxyfunctionalization
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