Application of Supercritical Fluid Extraction in Industrial Waste Treatment: Thermodynamic Modeling and Design

Boukouvalas, C; Magoulas, K; Tassios, D

dc.contributor.author	Boukouvalas, C	en
dc.contributor.author	Magoulas, K	en
dc.contributor.author	Tassios, D	en
dc.date.accessioned	2014-03-01T01:13:35Z
dc.date.available	2014-03-01T01:13:35Z
dc.date.issued	1998	en
dc.identifier.issn	0149-6395	en
dc.identifier.uri	https://dspace.lib.ntua.gr/xmlui/handle/123456789/12589
dc.subject	Industrial Waste	en
dc.subject	Supercritical Fluid Extraction	en
dc.subject	Thermodynamic Model	en
dc.subject.classification	Chemistry, Multidisciplinary	en
dc.subject.classification	Engineering, Chemical	en
dc.subject.other	Carbon dioxide	en
dc.subject.other	Industrial waste treatment	en
dc.subject.other	Mathematical models	en
dc.subject.other	Phenols	en
dc.subject.other	Solvents	en
dc.subject.other	Thermodynamics	en
dc.subject.other	Wastewater treatment	en
dc.subject.other	Water	en
dc.subject.other	Cresol	en
dc.subject.other	Supercritical fluid extraction	en
dc.subject.other	extraction	en
dc.subject.other	supercritical fluid	en
dc.subject.other	waste water	en
dc.title	Application of Supercritical Fluid Extraction in Industrial Waste Treatment: Thermodynamic Modeling and Design	en
heal.type	journalArticle	en
heal.identifier.primary	10.1080/01496399808544775	en
heal.identifier.secondary	http://dx.doi.org/10.1080/01496399808544775	en
heal.language	English	en
heal.publicationDate	1998	en
heal.abstract	The use of supercritical fluid extraction (SFE) as a separation process for the treatment of industrial wastewater is examined, The performance of the LCVM EoS/G(E) model in thermodynamic modeling of the systems CO2/H2O/organic pollutant (aromatics, phenol, cresol), including the presence of a cosolvent, is evaluated. The design of a unit that processes the water/phenol system with carbon dioxide, with and without a cosolvent, is also examined. The use of a cosolvent is a very important parameter for the SFE process since it can cause a significant decrease in the total cost of the unit. Application of the process appears limited due to the lack of predictive models and the high cost of equipment.	en
heal.publisher	MARCEL DEKKER INC	en
heal.journalName	Separation Science and Technology	en
dc.identifier.doi	10.1080/01496399808544775	en
dc.identifier.isi	ISI:000072274200007	en
dc.identifier.volume	33	en
dc.identifier.issue	3	en
dc.identifier.spage	387	en
dc.identifier.epage	410	en