Liquid–liquid equilibria of the systems dipropyl ether+n-propanol+water and dipropyl ether+n-propanol+ethylene glycol at different temperatures
Author:
Publisher
Elsevier BV
Subject
Physical and Theoretical Chemistry,General Physics and Astronomy,General Chemical Engineering
Reference16 articles.
1. Isobaric vapor–liquid equilibria for the binary systems 1-propyl alcohol+dipropyl ether and 1-butyl alcohol+dibutyl ether at 20 and 101.3kPa
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3. Conceptual Desing of Distillation Systems;Doherty,2001
4. Vapor–liquid equilibria in the ternary system dipropyl ether+1-propanol+1-pentanol and the binary systems dipropyl ether+1-pentanol, 1-propanol+1-pentanol at 101.3kPa
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1. Measurement and correlation of the (p, ρ, T) behaviour of liquid ethylene glycol at temperatures from (283.3 to 393.1) K and pressures up to 100.1 MPa;The Journal of Chemical Thermodynamics;2020-05
2. Reversible Reaction-Assisted Intensification Process for Separating the Azeotropic Mixture of Ethanediol and 1,2-Butanediol: Vapor–Liquid Equilibrium and Economic Evaluation;Industrial & Engineering Chemistry Research;2018-03-21
3. Liquid–Liquid Equilibrium for Ternary System n-Butanol + n-Hexane + Ethylene Glycol at 298.15–323.15 K;Journal of Chemical & Engineering Data;2017-12-08
4. Liquid-liquid extraction data of methyl ethyl ketone from n-hexane using ethylene glycol at 298.15–313.15 K;Journal of Molecular Liquids;2017-11
5. Dehydration of n-propanol and methanol to produce etherified fuel additives;AIMS Energy;2017
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