Vapor Liquid Equilibria for Acetic Acid–Acetaldehyde–Crotonaldehyde System: Gibbs Ensemble Molecular Simulation for Pure Components and Binary Systems and NRTL Model Prediction for Ternary System-Reference-Cited by-同舟云学术

Vapor Liquid Equilibria for Acetic Acid–Acetaldehyde–Crotonaldehyde System: Gibbs Ensemble Molecular Simulation for Pure Components and Binary Systems and NRTL Model Prediction for Ternary System

Published:2018-01-30 Issue:6 Volume:57 Page:2353-2364
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

Zhang Minhua¹²^ORCID,Chen Lihang¹²,Yang Huaming¹²,Ma Jing¹²^ORCID

Affiliation:

1. Key Laboratory for Green Chemical Technology of Ministry of Education, R&D Center for Petrochemical Technology, Tianjin University, Tianjin 300072, China

2. Collaborative Innovation Center of Chemical Science and Engineering, Tianjin University, Tianjin 300072, China

Funder

National Natural Science Foundation 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.7b04688

Reference37 articles.

1. Activity and deactivation of a catalyst for vinyl acetate synthesis in an industrial fluidized reactor

2. Geometric Structures of Associating Component Optimized toward Correlation and Prediction of Isobaric Vapor–Liquid Equilibria for Binary and Ternary Mixtures of Ethanal, Ethanol, and Ethanoic Acid

3. Gleichgewicht Flüssigkeit-Dampf XXXI. Systeme Acetaldehyd-Essigsäure und Acetaldehyd-Vinylacetat

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