HYDROISOMERIZATION AND HYDROCRACKING OF ALKANES - INFLUENCE OF THE BALANCE BETWEEN ACID AND HYDROGENATING FUNCTIONS ON THE TRANSFORMATION OF N-DECANE ON PTHY CATALYSTS

Citation
F. Alvarez et al., HYDROISOMERIZATION AND HYDROCRACKING OF ALKANES - INFLUENCE OF THE BALANCE BETWEEN ACID AND HYDROGENATING FUNCTIONS ON THE TRANSFORMATION OF N-DECANE ON PTHY CATALYSTS, Journal of catalysis, 162(2), 1996, pp. 179-189
Citations number
29
Categorie Soggetti
Chemistry Physical
Journal title
ISSN journal
00219517
Volume
162
Issue
2
Year of publication
1996
Pages
179 - 189
Database
ISI
SICI code
0021-9517(1996)162:2<179:HAHOA->2.0.ZU;2-V
Abstract
The transformation of n-decane was studied at 473 K, 101 kPa and p(H2) /p(n-decane) = 9 on a series of PtHY catalysts containing from 0.02 to 1.5 wt% platinum and with Si/Al atomic ratios of 3, 9, or 35. The rat io between the number of accessible Pt atoms and the number of acid si tes on which the heat of ammonia adsorption is greater than 100 kJ mol (-1) (n(Pt)/n(A)) was chosen for characterizing the balance between th e hydrogenating and the acid functions. The activities, stabilities, a nd selectivities of the catalysts are definitely governed by this bala nce. For low values of n(Pt)/n(A) (< 0.03), the activity per acid site is low, the deactivation is rapid and n-decane leads directly to all the isomerization and cracking products. For high values (greater than or equal to 0.17) the activity per acid site is maximal, the deactiva tion is very slow and n-decane transforms successively into monobranch ed isomers, dibranched isomers, and tribranched isomers plus cracking products. In this latter case the catalyst can be considered as an ide al bifunctional catalyst, namely a catalyst on which only one transfor mation of the alkene intermediates on the acid sites can occur during their diffusion from the platinum sites on which they are generated to those on which they are hydrogenated. Therefore the reaction scheme o f n-decane transformation matches the reaction scheme of olefinic inte rmediates. From the product distribution established on ideal catalyst s the mechanism of the transformation of olefinic intermediates can be deduced. Branching isomerization occurs through protonated cyclopropa ne and cyclobutane intermediates. The cracking products result from th e beta-scission steps of tribranched decenes which involve two tertiar y carbenium ion intermediates (mode A) and from the beta-scission step s of dibranched decenes which involve one tertiary and one secondary c arbenium ion intermediate (mode B). The participation of the beta-scis sion of mono, di, and tribranched decenes through mode C (via two seco ndary carbenium ion intermediates) is negligible. The rate constants o f the various steps involved in n-decane transformation are estimated. They can be classified in the following order: A cracking > Methyl sh ift > Branching > B cracking much greater than C cracking. (C) 1996 Ac ademic Press, Inc.