On the important of non-ideal flow effects in the operation of industrial-scale adiabatic membrane reactors

Koukou, MK; Papayannakos, N; Markatos, NC

dc.contributor.author	Koukou, MK	en
dc.contributor.author	Papayannakos, N	en
dc.contributor.author	Markatos, NC	en
dc.date.accessioned	2014-03-01T01:16:50Z
dc.date.available	2014-03-01T01:16:50Z
dc.date.issued	2001	en
dc.identifier.issn	1385-8947	en
dc.identifier.uri	https://dspace.lib.ntua.gr/xmlui/handle/123456789/14254
dc.subject	Industrial-scale	en
dc.subject	Membrane	en
dc.subject	Module design	en
dc.subject	Non-ideal flow	en
dc.subject.classification	Engineering, Chemical	en
dc.subject.other	carbon dioxide	en
dc.subject.other	flow kinetics	en
dc.subject.other	fluid flow	en
dc.subject.other	gas emission	en
dc.subject.other	gasification	en
dc.subject.other	mathematical model	en
dc.subject.other	membrane reactor	en
dc.subject.other	suspension	en
dc.subject.other	Carbon dioxide	en
dc.subject.other	Computer simulation	en
dc.subject.other	Gasification	en
dc.subject.other	Mathematical techniques	en
dc.subject.other	Adiabatic membrane reactors	en
dc.subject.other	Chemical engineering	en
dc.subject.other	dispersion	en
dc.subject.other	flow	en
dc.subject.other	mathematical modeling	en
dc.subject.other	membrane	en
dc.subject.other	reactor	en
dc.title	On the important of non-ideal flow effects in the operation of industrial-scale adiabatic membrane reactors	en
heal.type	journalArticle	en
heal.identifier.primary	10.1016/S1385-8947(00)00243-6	en
heal.identifier.secondary	http://dx.doi.org/10.1016/S1385-8947(00)00243-6	en
heal.language	English	en
heal.publicationDate	2001	en
heal.abstract	A mathematical model taking into account mass dispersion is presented for the simulation of the performance of an adiabatic full-scale membrane reactor. Results are presented from the application of this model to a membrane reactor, that is introduced in an integrated gasification combined cycle plant, to control carbon dioxide emissions. The performance of this reactor equipped with highly selective membranes is studied in detail. The extent of the impact of the non-ideal flow effects on the membrane reactor operation is discussed. It is shown that dispersion effects have a negative influence on the performance of industrial-scale membrane reactors and they must be considered as a basic parameter to their design. (C) 2001 Elsevier Science B.V. All rights reserved.	en
heal.publisher	ELSEVIER SCIENCE SA	en
heal.journalName	Chemical Engineering Journal	en
dc.identifier.doi	10.1016/S1385-8947(00)00243-6	en
dc.identifier.isi	ISI:000168793600004	en
dc.identifier.volume	83	en
dc.identifier.issue	2	en
dc.identifier.spage	95	en
dc.identifier.epage	105	en