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

Spiliotis, N; Magoulas, K; Tassios, D

dc.contributor.author	Spiliotis, N	en
dc.contributor.author	Magoulas, K	en
dc.contributor.author	Tassios, D	en
dc.date.accessioned	2014-03-01T01:10:08Z
dc.date.available	2014-03-01T01:10:08Z
dc.date.issued	1994	en
dc.identifier.issn	0378-3812	en
dc.identifier.uri	https://dspace.lib.ntua.gr/xmlui/handle/123456789/11322
dc.subject	Correlation	en
dc.subject	Cubic	en
dc.subject	Equation of state	en
dc.subject	Excess functions	en
dc.subject	Group contribution	en
dc.subject	Hydrocarbons	en
dc.subject	Prediction	en
dc.subject	Solid-fluid equilibria	en
dc.subject	Solubility	en
dc.subject	Theory	en
dc.subject	Vapor-liquid equilibria	en
dc.subject.classification	Thermodynamics	en
dc.subject.classification	Chemistry, Physical	en
dc.subject.classification	Engineering, Chemical	en
dc.subject.other	Aromatic hydrocarbons	en
dc.subject.other	Carbon dioxide	en
dc.subject.other	Equations of state of liquids	en
dc.subject.other	Forecasting	en
dc.subject.other	Phase equilibria	en
dc.subject.other	Supercritical fluid extraction	en
dc.subject.other	Excess functions	en
dc.subject.other	Mole fraction values	en
dc.subject.other	Solid fluid equilibria	en
dc.subject.other	Solid vapor pressures	en
dc.subject.other	Thermosensitive substances	en
dc.subject.other	Vapor liquid equilibria	en
dc.subject.other	Solubility	en
dc.title	Prediction of the solubility of aromatic hydrocarbons in supercritical CO2 with EoSGE models	en
heal.type	journalArticle	en
heal.identifier.primary	10.1016/0378-3812(94)87072-1	en
heal.identifier.secondary	http://dx.doi.org/10.1016/0378-3812(94)87072-1	en
heal.language	English	en
heal.publicationDate	1994	en
heal.abstract	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
heal.publisher	ELSEVIER SCIENCE BV	en
heal.journalName	Fluid Phase Equilibria	en
dc.identifier.doi	10.1016/0378-3812(94)87072-1	en
dc.identifier.isi	ISI:A1994QG35400002	en
dc.identifier.volume	102	en
dc.identifier.issue	2	en
dc.identifier.spage	121	en
dc.identifier.epage	141	en