| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 6643622 | Fuel | 2012 | 12 Pages |
Abstract
⺠Benzene used as co-reactant in the dehydrogenation of heavy paraffins improves conversion and catalyst stability. ⺠Swing trickle bed reactors coupled with catalyst regeneration provides higher yield of olefins than gas phase reactors. ⺠PtCu on structured alumina working in liquid phase produces more terminal olefins than conventional Pt/alumina catalyst. ⺠The dehydrogenation product used without fractionation in the alkylation stage for LAB productionshows promising results.
Keywords
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Chemical Engineering (General)
Authors
Alexis Lira, Roberto Galiasso Tailleur,