Isothermal Vapor−Liquid Equilibria for Binary Mixtures of Carbon Dioxide with Hexyl Acetate, Cyclohexyl Acetate, or Phenyl Acetate at Elevated Pressures-Reference-Cited by-同舟云学术

Isothermal Vapor−Liquid Equilibria for Binary Mixtures of Carbon Dioxide with Hexyl Acetate, Cyclohexyl Acetate, or Phenyl Acetate at Elevated Pressures

Published:2001-09-13 Issue:6 Volume:46 Page:1410-1414
ISSN:0021-9568
Container-title:Journal of Chemical & Engineering Data
language:en
Short-container-title:J. Chem. Eng. Data

Author:

Lee Ming-Jer¹,Chen Wen-Sheng¹,Lin Ho-mu¹

Affiliation:

1. Department of Chemical Engineering, National Taiwan University of Science and Technology, 43 Keelung Road, Section 4, Taipei 106-07, Taiwan

Publisher

American Chemical Society (ACS)

Subject

General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/je010036m

Reference18 articles.

1. Equilibrium constants from a modified Redlich-Kwong equation of state

2. Creation and Survival of Secondary Crystal Nuciel. The Potassium Sulfate-Water System

3. A new cubic equation of state for fluids and fluid mixtures

4. High pressure phase behavior in systems containing CO2 and heavier compounds with similar vapor pressures

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