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High Pressure Vapour-Liquid Equilibrium of Volatiles in Supercritical Carbon Dioxide

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Gurgenova K., Bogeł-Łukasik R., Wawrzyniak P.
Chemical and Process Engineering
|
2013
|
vol. 34
|
issue 3
387-392
EN
Binary vapour-liquid equilibrium of thymoquinone and carbon dioxide at the isothermal conditions was carried out at temperature 323.15 K and pressures from 6 to 10 MPa. The experimental data were fitted to the Soave-Redlich-Kwong equation of state. Results could be used for selection of process parameters in separation of volatiles from raw oil or for evaluation of existing separation technologies.
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