Liquid–Liquid Phase Equilibria for the Ternary Water + Acetic Acid + 3,3-Dimethyl-2-butanone System at (298.15, 313.15 and 323.15) K-Reference-Cited by-同舟云学术

Liquid–Liquid Phase Equilibria for the Ternary Water + Acetic Acid + 3,3-Dimethyl-2-butanone System at (298.15, 313.15 and 323.15) K

Published:2015-10-02 Issue:11 Volume:60 Page:3187-3192
ISSN:0021-9568
Container-title:Journal of Chemical & Engineering Data
language:en
Short-container-title:J. Chem. Eng. Data

Author:

Liu Dong¹,Li Libo¹,Luo Liejin¹,Chen Yun¹

Affiliation:

1. Key Laboratory of Heat Transfer Enhancement and Energy Conservation of Ministry of Education, School of Chemistry and Chemical Engineering, South China University of Technology, Guangzhou, 510640, P. R. China

Funder

Guangzhou Municipality

Guandong Natural Science Foundation

South China University of Technology

National Natural Science Foundation of China

Ministry of Education of the People's Republic of China

Publisher

American Chemical Society (ACS)

Subject

General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/acs.jced.5b00370

Reference24 articles.

1. Liquid−Liquid Equilibria of the Ternary System Water + Acetic Acid + 2-Methyl-2-butanol

2. Liquid-liquid equilibrium for the ternary systems composed of diethyl phenylmalonate + acetic acid + water and diethyl methylmalonate + acetic acid + water at 294, 298, and 308 K

3. Liquid−Liquid Equilibria of the Ternary Systems Water + Acetic Acid + Ethyl Acetate and Water + Acetic Acid + Isophorone (3,5,5-Trimethyl-2-cyclohexen-1-one)

4. Liquid–Liquid Equilibria for the System Water + 4-Methylpentan-2-one + Acetic Acid at Several Temperatures

5. Liquid−Liquid Equilibria of the System Water + Acetic Acid + 2-Hexanone at 25 °C and 35 °C

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3. Phase Equilibrium Measurement and Thermodynamic Modeling of the 4-Methylpentan-2-one/3-Methylphenol, and 4-Methylphenol/Water Ternary Systems at 298.2, 313.2, and 323.2 K and 0.1 MPa;Journal of Chemical & Engineering Data;2016-12-22