HEAL DSpace

Axial dispersion and hold-up in a bench-scale trickle-bed reactor at operating conditions

Αποθετήριο DSpace/Manakin

Εμφάνιση απλής εγγραφής

dc.contributor.author Tsamatsoulis, D en
dc.contributor.author Papayannakos, N en
dc.date.accessioned 2014-03-01T01:09:44Z
dc.date.available 2014-03-01T01:09:44Z
dc.date.issued 1994 en
dc.identifier.issn 0009-2509 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/11166
dc.subject Operant Conditioning en
dc.subject.classification Engineering, Chemical en
dc.subject.other Catalysis en
dc.subject.other Catalysts en
dc.subject.other Chemical engineering en
dc.subject.other Flow of fluids en
dc.subject.other Liquids en
dc.subject.other Mathematical models en
dc.subject.other Packed beds en
dc.subject.other Particles (particulate matter) en
dc.subject.other Velocity en
dc.subject.other Axial dispersion en
dc.subject.other Bench scale reactors en
dc.subject.other Catalytic hydrotreatment en
dc.subject.other Hold up en
dc.subject.other Trickle bed reactors en
dc.subject.other Chemical reactors en
dc.subject.other Flow en
dc.subject.other Reactors en
dc.subject.other Trickle-Bed en
dc.title Axial dispersion and hold-up in a bench-scale trickle-bed reactor at operating conditions en
heal.type journalArticle en
heal.identifier.primary 10.1016/0009-2509(94)80052-9 en
heal.identifier.secondary http://dx.doi.org/10.1016/0009-2509(94)80052-9 en
heal.language English en
heal.publicationDate 1994 en
heal.abstract Response curves of a tracer step increase and decrease were derived and used to evaluate liquid flow non-idealities and hold-up in a bench-scale reactor by the axial dispersion model. Real feeds and operating conditions used in catalytic hydrotreatment were employed in experimentation. Diluted and non-diluted beds were prepared with non-porous extrudates of commercial catalyst dimensions and crushed particles. Three types of boundary conditions were tested to estimate axial dispersion coefficients and hold-up. The dependence of DZ and hL on the bed particle size and liquid velocity is examined. Bo was found to be a function of bed characteristics. © 1993. en
heal.publisher PERGAMON-ELSEVIER SCIENCE LTD en
heal.journalName Chemical Engineering Science en
dc.identifier.doi 10.1016/0009-2509(94)80052-9 en
dc.identifier.isi ISI:A1994MP98600008 en
dc.identifier.volume 49 en
dc.identifier.issue 4 en
dc.identifier.spage 523 en
dc.identifier.epage 529 en


Αρχεία σε αυτό το τεκμήριο

Αρχεία Μέγεθος Μορφότυπο Προβολή

Δεν υπάρχουν αρχεία που σχετίζονται με αυτό το τεκμήριο.

Αυτό το τεκμήριο εμφανίζεται στην ακόλουθη συλλογή(ές)

Εμφάνιση απλής εγγραφής