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Membrane reactor modelling: A comparative study to evaluate the role of combined mass and heat dispersion in large-scale adiabatic membrane modules

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dc.contributor.author Markatos, NC en
dc.contributor.author Vogiatzis, E en
dc.contributor.author Koukou, MK en
dc.contributor.author Papayannakos, N en
dc.date.accessioned 2014-03-01T01:22:44Z
dc.date.available 2014-03-01T01:22:44Z
dc.date.issued 2005 en
dc.identifier.issn 0263-8762 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/16637
dc.subject Ceramic membrane en
dc.subject Heat dispersion en
dc.subject Industrial-scale en
dc.subject Mass dispersion en
dc.subject Membrane reactor en
dc.subject Module design en
dc.subject.classification Engineering, Chemical en
dc.subject.other Boundary conditions en
dc.subject.other Catalysis en
dc.subject.other Ceramic materials en
dc.subject.other Heat transfer en
dc.subject.other Mass transfer en
dc.subject.other Mathematical models en
dc.subject.other Membranes en
dc.subject.other Particles (particulate matter) en
dc.subject.other Process control en
dc.subject.other Adiabatic membrane modules en
dc.subject.other Ceramic membrane en
dc.subject.other Heat dispersion en
dc.subject.other Mass dispersion en
dc.subject.other Membrane reactor modelling en
dc.subject.other Module design en
dc.subject.other Water gas shift reaction (WGS) en
dc.subject.other Chemical reactors en
dc.subject.other ceramic membrane en
dc.subject.other heat transfer en
dc.subject.other mass transfer en
dc.title Membrane reactor modelling: A comparative study to evaluate the role of combined mass and heat dispersion in large-scale adiabatic membrane modules en
heal.type journalArticle en
heal.identifier.primary 10.1205/cherd.04299 en
heal.identifier.secondary http://dx.doi.org/10.1205/cherd.04299 en
heal.language English en
heal.publicationDate 2005 en
heal.abstract In this work, the combined role of mass and heat dispersion effects on the performance of adiabatic large-scale membrane reactor modules is investigated. The model developed can be used in predicting membrane reactor performance under industrial process conditions. The membrane reactor configuration adopted in this study assumes that the water gas shift reaction (WGS) takes place in the feed side of the membrane reactor that is filled with catalytic particles. The membrane reactor is equipped with a highly selective ceramic membrane. To undertake a systematic analysis of the role of mass and heat dispersion on the performance of the WGS membrane reactor, various versions of a two-dimensional model have been applied. It is shown that none of the mass and heat dispersion effects can be neglected a priori and their impact on the membrane reactor operation depends on the process characteristics. © 2005 Institution of Chemical Engineers. en
heal.publisher INST CHEMICAL ENGINEERS en
heal.journalName Chemical Engineering Research and Design en
dc.identifier.doi 10.1205/cherd.04299 en
dc.identifier.isi ISI:000233456000002 en
dc.identifier.volume 83 en
dc.identifier.issue 10 A en
dc.identifier.spage 1171 en
dc.identifier.epage 1178 en


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