Coking and deactivation during n-hexane cracking in ultrastable zeolite Y

Citation
B. Paweewan et al., Coking and deactivation during n-hexane cracking in ultrastable zeolite Y, APP CATAL A, 185(2), 1999, pp. 259-268
Citations number
67
Categorie Soggetti
Physical Chemistry/Chemical Physics","Chemical Engineering
Journal title
APPLIED CATALYSIS A-GENERAL
ISSN journal
0926860X → ACNP
Volume
185
Issue
2
Year of publication
1999
Pages
259 - 268
Database
ISI
SICI code
0926-860X(19990920)185:2<259:CADDNC>2.0.ZU;2-H
Abstract
A multi-technique approach has been used to investigate coke formation and the effects of coke formation during n-hexane cracking on ultrastable zeoli te Y. The product analysis reveals that propane and propene are the major p roducts, and this suggests that the reaction initiation step may be direct protonation at very strong Bronsted acid sites. The coke formed does not ch ange in composition significantly over the course of the reaction. Infrared spectroscopy reveals that the vast majority of Bronsted and Lewis acid sit es are still present in the catalyst, even when the catalyst activity has b ecome low. Diffusion measurements using pulsed field gradient (PFG) NMR sho w that the mobility of adsorbed n-butane or n-hexane is not affected by the presence of the coke, and so shows that pore blockage is not a significant factor. Based on the experimental results, it is argued that selective sit e poisoning of a few very strong acid sites is the main deactivation mechan ism for this reaction under the conditions employed. (C) 1999 Elsevier Scie nce B.V. All rights reserved.