Isobaric (Vapor + Liquid) Equilibria for Propylene Carbonate with para-Xylene, ortho-Xylene, meta-Xylene, and Ethylbenzene at 101.33 kPa
Author:
Affiliation:
1. State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Qingdao 266580, China
2. Yantai Guobang Chemical Machine Technology Co., Ltd., Yantai 264004, China
Funder
National Natural Science Foundation of China
Publisher
American Chemical Society (ACS)
Subject
General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/acs.jced.3c00076
Reference32 articles.
1. Ternary (Liquid + Liquid) Equilibrium Experiment and Thermodynamic Modeling for Solvents (p-Xylene, Mesityl Oxide) + 2-Butanone + Water at 298.2, 303.2, and 313.2 K under 101.3 kPa
2. Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
3. Isobaric vapor–liquid equilibrium of the binary system sec-butyl acetate +para-xylene and the quaternary system methyl acetate +para-xylene +sec-butyl acetate + acetic acid at 101.3 kPa
4. Vapor–liquid equilibrium of binary CO2–organic solvent systems (ethanol, tetrahydrofuran, ortho-xylene, meta-xylene, para-xylene)
5. Selectivities at infinite dilution of xylene isomers in ionic liquids
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