Phase Equilibrium Properties of the 1-Phenylethanol−Carbon Dioxide and 2-Octanol−Carbon Dioxide Binary Systems at 303.15 K, 313.15 K, and 323.15 K
Phase equilibria data for the 1-phenylethanol−CO2 and 2-octanol−CO2 systems were measured at 303.15 K, 313.15 K, and 323.15 K and at pressures up to 145 bar. An equilibrium cell with circulating gas phase was used for the measurements. Data were correlated with the Peng−Robinson equation of state. D...
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Published in | Journal of chemical and engineering data Vol. 46; no. 1; pp. 117 - 119 |
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Main Authors | , |
Format | Journal Article |
Language | English |
Published |
Washington, DC
American Chemical Society
01.01.2001
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Subjects | |
Online Access | Get full text |
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Summary: | Phase equilibria data for the 1-phenylethanol−CO2 and 2-octanol−CO2 systems were measured at 303.15 K, 313.15 K, and 323.15 K and at pressures up to 145 bar. An equilibrium cell with circulating gas phase was used for the measurements. Data were correlated with the Peng−Robinson equation of state. Different methods were tested for calculating the binary interaction parameters k ij and l ij of the quadratic mixing rules. |
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Bibliography: | istex:CCB122060346B63D750C3631B44A6744B575F069 ark:/67375/TPS-S50QXMVQ-F |
ISSN: | 0021-9568 1520-5134 |
DOI: | 10.1021/je990306p |