Isothermal Vapor−Liquid Equilibria for the Binary System of Carbon Dioxide (CO2) + 1,1,1,2,3,3,3-Heptafluoropropane (R-227ea)-Reference-Cited by-同舟云学术

Isothermal Vapor−Liquid Equilibria for the Binary System of Carbon Dioxide (CO2) + 1,1,1,2,3,3,3-Heptafluoropropane (R-227ea)

Published:2010-10-26 Issue:11 Volume:55 Page:4999-5003
ISSN:0021-9568
Container-title:Journal of Chemical & Engineering Data
language:en
Short-container-title:J. Chem. Eng. Data

Author:

Kim Seol A.¹,Lim Jong Sung¹,Kang Jeong Won¹

Affiliation:

1. Department of Chemical and Biomolecular Engineering, Sogang University, CPO Box 1142, Seoul 100-611, South Korea, and Department of Chemical and Biological Engineering, Korea University, 5-Ga Anam-Dong, Sungbuk-Ku, Seoul 136-701, South Korea

Publisher

American Chemical Society (ACS)

Subject

General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/je100583z

Reference15 articles.

1. Interactions between protection of the ozone layer and global warming

2. Vapor–liquid equilibria of the 1,1-difluoroethane (HFC-152a)+isobutene system

3. Speed of sound, ideal-gas heat capacity at constant pressure, and second virial coefficients of HFC-227ea

4. (Vapor+liquid) equilibrium data for (carbon dioxide+1,1-difluoroethane) system at temperatures from (258 to 343)K and pressures up to about 8MPa

5. VLE measurement for binary systems of CO2+1,1,1,2-tetrafluoroethane (HFC-134a) at high pressures

Cited by 7 articles. 订阅此论文施引文献订阅此论文施引文献，注册后可以免费订阅5篇论文的施引文献，订阅后可以查看论文全部施引文献

1. Vapor-liquid equilibria for binary systems carbon dioxide + 1,1,1,2,3,3-hexafluoro-3-(2,2,2-trifluoroethoxy)propane or 1-ethoxy-1,1,2,2,3,3,4,4,4-nonafluorobutane at 303.15–323.15 K;Fluid Phase Equilibria;2020-12

2. Benchmark Database Containing Binary-System-High-Quality-Certified Data for Cross-Comparing Thermodynamic Models and Assessing Their Accuracy;Industrial & Engineering Chemistry Research;2020-07-17

3. High-pressure fluid-phase equilibria: Trends, recent developments, and systems investigated (2009–2012);Fluid Phase Equilibria;2019-04

4. Prediction of vapor–liquid equilibria for mixtures of low boiling point compounds using Wong–Sandler mixing rule and EOS/GE model;Chemical Engineering Science;2016-10

5. A simple model for temperature-independent k of the PR-vdW model for mixtures containing HCs, HFCs, PFCs, HFOs, CO2, RE170 and R13I1;Fluid Phase Equilibria;2016-10