Liquid–Liquid Equilibrium of Isobutyl Acetate + Isobutyl Alcohol + Imidazolium-Based Ionic Liquids at 298.15 and 308.15 K
Author:
Affiliation:
1. College of Chemical and Environmental Engineering, Shandong University of Science and Technology, Qingdao 266590, China
2. College of Chemical Engineering, Qingdao University of Science and Technology, Qingdao 266042, China
Funder
Shandong Province
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.8b01045
Reference39 articles.
1. Isobaric VLE at 0.6MPa for binary systems Isobutyl Acetate+Ethanol, +1-Propanol or +2-Propanol
2. Separation of isobutyl alcohol and isobutyl acetate by extractive distillation and pressure-swing distillation: Simulation and optimization
3. Isobaric vapor–liquid equilibria for the binary systems isobutyl alcohol+isobutyl acetate and tert-butyl alcohol+tert-butyl acetate at 20 and 101.3kPa
4. Separation of benzene and cyclohexane by extractive distillation intensified with ionic liquid
5. Isobaric vapour–liquid equilibrium measurements and extractive distillation process for the azeotrope of ( N , N -dimethylisopropylamine + acetone)
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