Using tert-Butyl Alcohol as an Adductive Agent for Separation of an m-Cresol and 2,6-Xylenol Mixture
Author:
Affiliation:
1. Department of Chemical Engineering, National Central University, Chung-li, 32054, Taiwan
Publisher
American Chemical Society (ACS)
Subject
Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/ie990759n
Reference17 articles.
1. (Solid + liquid) phase equilibria in binary mixtures containing benzene, a cycloalkane, an n-alkane, or tetrachloromethane An equation for representing (solid + liquid) phase equilibria
2. Solid-liquid equilibria for solvated nonelectrolyte mixtures
3. Local compositions in thermodynamic excess functions for liquid mixtures
4. Separation of m-cresol and p-cresol by extractive crystallization
5. Separation of close boiling point mixtures (p-cresol/m-cresol, guaiacol/alkylphenols, 3-picoline/4-picoline, substituted anilines) through dissociation extractive crystallization
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1. Purification of p-Cresol, o-Cresol, m-Cresol, and 2,6-Xylenol from the Quaternary Mixture by Three-Phase Crystallization;Industrial & Engineering Chemistry Research;2023-05-15
2. Chemical removal of m-cresol: a critical review;Reviews in Chemical Engineering;2021-07-22
3. Chemical Kinetics of the Alkylation of Xylenol for the Separation of Their Close-Boiling Isomers from Coal Tar;Petroleum Chemistry;2020-11
4. Experimental and Predicted Vapor–Liquid Equilibrium for Diisopropanolamine with m-Cresol and 2,6-Dimethylphenol at 20.0 kPa;Journal of Chemical & Engineering Data;2018-04-04
5. Measurement and correlation of isobaric vapour–liquid equilibrium for systems of o-cresol, m-cresol and 2, 6-dimethylphenol at 20.0 kPa;Fluid Phase Equilibria;2018-03
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