Vapor−Liquid Equilibria of the Carbon Dioxide + Acetone System at Pressures from (2.36 to 11.77) MPa and Temperatures from (333.15 to 393.15) K

High-pressure phase equilibrium data p, T, x, ρ, and V m for the binary carbon dioxide + acetone system were measured at several temperatures (333.15, 353.15, 373.15, and 393.15) K and pressures from (2.36 to 11.77) MPa. The experimental data at 333.15 K are in good agreement with literature data, a...

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Bibliographic Details
Published inJournal of chemical and engineering data Vol. 50; no. 1; pp. 36 - 39
Main Authors Han, Fang, Xue, Yuan, Tian, Yiling, Zhao, Xuefeng, Chen, Li
Format Journal Article
LanguageEnglish
Published Washington, DC American Chemical Society 13.01.2005
Subjects
Chemistry
Exact sciences and technology
General and physical chemistry
Liquid-vapor equilibria
Phase equilibria
Binary mixture
Correlation
Equations of state
Carbon dioxide
Liquid vapor equilibrium
Ketone
Phase equilibrium
Acetone
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Summary:High-pressure phase equilibrium data p, T, x, ρ, and V m for the binary carbon dioxide + acetone system were measured at several temperatures (333.15, 353.15, 373.15, and 393.15) K and pressures from (2.36 to 11.77) MPa. The experimental data at 333.15 K are in good agreement with literature data, and the experimental results are correlated by the Peng−Robinson equation.
Bibliography:istex:90BA548DFEECC2C31455F75F851617E4BD986116
ark:/67375/TPS-8XBS7VXP-D
ISSN:0021-9568
1520-5134
DOI:10.1021/je049887v