Reversible Reaction-Assisted Intensification Process for Separating the Azeotropic Mixture of Ethanediol and 1,2-Butanediol: Vapor–Liquid Equilibrium and Economic Evaluation-Reference-Cited by-同舟云学术

Reversible Reaction-Assisted Intensification Process for Separating the Azeotropic Mixture of Ethanediol and 1,2-Butanediol: Vapor–Liquid Equilibrium and Economic Evaluation

Published:2018-03-21 Issue:14 Volume:57 Page:5083-5092
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

Li Hong¹,Zhao Zhenyu¹,Qin Jie¹,Wang Rui¹,Li Xingang¹,Gao Xin¹^ORCID

Affiliation:

1. School of Chemical Engineering and Technology, National Engineering Research Center of Distillation Technology, Collaborative Innovation Center of Chemical Science and Engineering (Tianjin), Tianjin University, Tianjin 300072, China

Funder

National Natural Science Foundation of China

National Key Research and Development Program of China

Publisher

American Chemical Society (ACS)

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/acs.iecr.7b04921

Reference39 articles.

1. Binary vapor–liquid equilibrium of methyl glycolate and ethylene glycol

2. Energy-Saving Designs for Separation of a Close-Boiling 1,2-Propanediol and Ethylene Glycol Mixture

3. Design and optimization of dimethyl oxalate (DMO) hydrogenation process to produce ethylene glycol (EG)

4. Song, G. Study on the Separation of Glycol-Propanediol-Butanediol System Using Azeotropic Distillation. Thesis, Tianjin University, Tianjin, China, 2006.

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