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Influence of the catalyst chloriding on isomerization and hydrogenolysis of n-pentane on Pt/Al/sub 2/O/sub 3/ catalysts

Journal Article · · Ind. Eng. Chem., Prod. Res. Dev.; (United States)
DOI:https://doi.org/10.1021/i360070a006· OSTI ID:6916442

The influence of the catalysts chloriding on isomerization and hydrogenolysis of n-pentane on Pt/Al/sub 2/O/sub 3/ catalysts was studied at 300/sup 0/-436/sup 0/C in a pulse microreactor and a continuous-flow, bench-scale tubular reactor with 0.75 and 0.59Vertical Bar3< by wt Pt/Al/sub 2/O/sub 3/ commercial reforming catalysts that contained 0.03, 0.066, or 0.087Vertical Bar3< sulfur. Fully sulfided catalysts (Vertical Bar3: 0.072Vertical Bar3< sulfur) showed high and stable isomerization activity but low-sulfur samples were more active in hydrogenolysis. Chlorination of the catalysts with CCl/sub 4/ in hydrogen flow at 400/sup 0/C decreased n-pentane conversion, effectively suppressed hydrogenolysis, and increased isomerization selectivity to 100Vertical Bar3<. By contrast, catalyst treatment with gaseous hydrogen chloride to the same chlorine content (5-7Vertical Bar3< by wt), had only a minor effect on the catalyst activity and selectivity. Apparently, the deactivation of the Pt sites specifically responsible for hydrogenolysis is mainly due to sulfiding or the deposition of coke formed from CCl/sub 4/ and to a much lesser extent to their chlorination. CCl/sub 4/ treatment also enhances the acidity of the alumina support and thus accelerates olefin isomerization. Hydrogen chemisorption and desorption data were used to characterize the Pt surface of the catalysts and their selectivities.

Research Organization:
Rijksuniv. Gent
OSTI ID:
6916442
Journal Information:
Ind. Eng. Chem., Prod. Res. Dev.; (United States), Journal Name: Ind. Eng. Chem., Prod. Res. Dev.; (United States) Vol. 18:2; ISSN IEPRA
Country of Publication:
United States
Language:
English