dc.contributor.author |
Ammus, JM |
en |
dc.contributor.author |
Androutsopoulos, GP |
en |
dc.date.accessioned |
2014-03-01T01:39:13Z |
|
dc.date.available |
2014-03-01T01:39:13Z |
|
dc.date.issued |
1987 |
en |
dc.identifier.issn |
08885885 |
en |
dc.identifier.uri |
https://dspace.lib.ntua.gr/xmlui/handle/123456789/22616 |
|
dc.relation.uri |
http://www.scopus.com/inward/record.url?eid=2-s2.0-0023313697&partnerID=40&md5=7dd0e927be045ba4bd6f0e81ed850057 |
en |
dc.subject.other |
CATALYSTS - Cobalt Compounds |
en |
dc.subject.other |
CHEMICAL REACTIONS - Reaction Kinetics |
en |
dc.subject.other |
HYDROCARBONS - Desulfurization |
en |
dc.subject.other |
GREEK OIL RESIDUE |
en |
dc.subject.other |
HDS KINETIC STUDIES |
en |
dc.subject.other |
SPINNING BASKET REACTOR |
en |
dc.subject.other |
PETROLEUM, CRUDE |
en |
dc.title |
HDS kinetic studies on Greek oil residue in a spinning basket reactor |
en |
heal.type |
journalArticle |
en |
heal.publicationDate |
1987 |
en |
heal.abstract |
A spinning basket reactor was used to investigate the hydrodesulfurization (HDS) kinetics of Greek (Thasos) atmospheric residue. The effects of temperature (285-395°C), pressure (30-70 bar), and particle size (L̄p = 5.67 × 10-3-58.9 × 10-3 cm) upon the intrinsic reaction rate were determined. Two commercial HDS supported catalysts (Co-Mo/γ-Al2O3) differing in their chemical composition and physical structure were employed. It was shown that the overall HDS reaction rate was kinetically controlled when the pulverized catalyst was rotated at a rate of 2540 rpm. Parameters defined by a general lumped kinetic equation, incorporating a hydrogen inhibition term, were obtained for both catalysts. The following kinetic equations were developed: (i) catalyst HT-400 E, R1 = 2.799 × 1010 exp(-34970/RT)PH2CS1.9/(1 + 0.0036PH2); (ii) catalyst ICI-41-6, R2 = 4.962 × 1010 exp(-32590/ RT)PH2CS2.3/ (1 + 0.0050PH2). Evaluations of effectiveness factors and effective diffusion coefficients reported in this paper and associated with the use of particular catalyst pellet sizes were based on HDS standard experiments. © 1987 American Chemical Society. |
en |
heal.journalName |
Industrial and Engineering Chemistry Research |
en |
dc.identifier.volume |
26 |
en |
dc.identifier.issue |
3 |
en |
dc.identifier.spage |
494 |
en |
dc.identifier.epage |
501 |
en |