Prediction of the solubility of aromatic hydrocarbons in supercritical CO2 with EoSGE models

 
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1994 (EN)

Prediction of the solubility of aromatic hydrocarbons in supercritical CO2 with EoSGE models (EN)

Spiliotis, N (EN)
Tassios, D (EN)
Magoulas, K (EN)

Prediction of the solubility of liquid and solid aromatic hydrocarbons in supercritical CO2 with the recently proposed LCVM model and the MHV2 model is presented. Satisfactory results are obtained in the case of LCVM, considering in particular the uncertainty of experimental measurements at such low mole fraction values and the pure component properties involved. Correlation of existing data is also considered in order to determine the limits of our expectations for the prediction results, including cases where the required solid vapor pressures are not available. © 1994. (EN)

journalArticle (EN)

Vapor-liquid equilibria (EN)
Correlation (EN)
Theory (EN)
Solid-fluid equilibria (EN)
Carbon dioxide (EN)
Hydrocarbons (EN)
Aromatic hydrocarbons (EN)
Equations of state of liquids (EN)
Thermosensitive substances (EN)
Cubic (EN)
Solid vapor pressures (EN)
Thermodynamics (EN)
Engineering, Chemical (EN)
Phase equilibria (EN)
Supercritical fluid extraction (EN)
Excess functions (EN)
Prediction (EN)
Solubility (EN)
Mole fraction values (EN)
Solid fluid equilibria (EN)
Vapor liquid equilibria (EN)
Chemistry, Physical (EN)
Forecasting (EN)
Equation of state (EN)
Group contribution (EN)


Fluid Phase Equilibria (EN)

English

1994 (EN)

121 (EN)
10.1016/0378-3812(94)87072-1 (EN)
2 (EN)
102 (EN)
ISI:A1994QG35400002 (EN)
0378-3812 (EN)
141 (EN)

ELSEVIER SCIENCE BV (EN)




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