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Vapor-liquid equilibrium of binary CO2-organic solvent systems (ethanol, tetrahydrofuran, ortho-xylene, meta-xylene, para-xylene)Knez, Željko ...High pressure vapor-liquid phase equilibrium data (P-T-x-y) for the binary mixtures of organic solvent (ethanol, tetrahydrofuran, o-xylene, m-xylene, p-xylene) with CO2 have been measured at ... temperatures 313.2, 333.2, 353.2 K and pressures from 1 to 14 MPa using a static-analytic method. For the systemsethanol-CO2 and tetrahydrofuran-CO2, the experimental data at 313.2 and333.2 K are in a good agreement with literature data. The experimental results have been correlated by the Peng-Robinson equation of state in combination with van der Waals one fluid mixing rule with two adjustable parameters.Source: The Journal of supercritical fluids. - ISSN 0896-8446 (Vol. 43, iss. 3, 2008, str. 383-389)Type of material - article, component partPublish date - 2008Language - englishCOBISS.SI-ID - 11793686
Author
Knez, Željko |
Škerget, Mojca |
Ilić, Ljiljana, 1978- |
Lütge, Christoph, kemik
Topics
kemijska pro cesna tehnika |
visokotlačna tehnologija |
ogljikov dioksid |
etanol |
tetrahidrofuran |
ksilen |
fazno ravnotežje |
eksperimentalni podatki |
chemical processing |
high pressure technology |
carbon dioxide |
ethanol |
tetrahydrofuran |
xylene |
vapor-liquid equilibrium |
experimental data |
PR equation of state

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Database name | Field | Year |
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Links to authors' personal bibliographies | Links to information on researchers in the SICRIS system |
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Knez, Željko | 02619 |
Škerget, Mojca | 11865 |
Ilić, Ljiljana, 1978- | 29843 |
Lütge, Christoph, kemik | ![]() |
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