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 |