ETHYLBENZENE HYDROISOMERIZATION OVER BIFUNCTIONAL ZEOLITE BASED CATALYSTS - THE INFLUENCE OF FRAMEWORK AND EXTRAFRAMEWORK COMPOSITION AND ZEOLITE STRUCTURE
Ld. Fernandes et al., ETHYLBENZENE HYDROISOMERIZATION OVER BIFUNCTIONAL ZEOLITE BASED CATALYSTS - THE INFLUENCE OF FRAMEWORK AND EXTRAFRAMEWORK COMPOSITION AND ZEOLITE STRUCTURE, Journal of catalysis (Print), 177(2), 1998, pp. 363-377
The hydroisomerization of ethylbenzene (EB) has been carried out on a
series of bifunctional Pt/Al2O3-zeolite catalysts, in which both the s
tructure (mordenite, beta, Y, ZSM-5, MCM-22) and the chemical composit
ion (for the mordenite and beta samples) of the zeolitic component wer
e varied. Postsynthesis methods such as ion-exchange, steaming and che
mical treatments were used to modify the composition of the samples (f
ramework and extraframework Al content and nature of the compensation
cation). Both parameters, zeolite structure and chemical composition,
were seen to affect the activity and selectivity of the resultant cata
lysts. Large pore zeolites, particularly mordenite and beta, presented
the highest selectivity to the desired isomerization products, i.e.,
xylenes. In the case of mordenites the textural properties (mainly the
mesoporosity), played a key role in determining the activity and sele
ctivity of the catalysts. Both, zeolite acidity and mesoporosity deter
mined the amount of Bronsted sites accessible to the reactant molecule
s. It was seen that a reduced amount of accessible Bronsted acid sites
in the zeolite favored the isomerization of EB with respect to second
ary reactions like cracking of the naphthenes and dealkylation. Select
ivities to xylenes above 40% at 60% EB conversion were obtained with m
ost of the mordenite-based catalysts. Also, the calcium-exchanged mord
enite samples gave larger xylene yields than the corresponding protoni
c samples. In the case of the Pt/Al2O3-beta samples, it was seen that
formation of xylenes by isomerization of EB is favored in catalysts pr
esenting a reduced density of Bronsted acid sites and a high mesoporos
ity. Thus, those catalysts prepared from the beta samples obtained by
steaming and steaming + acid treatment of the original acidic zeolite
were the most selective to xylenes, giving a selectivity close to 40%
at ca 60% EB conversion. (C) 1998 Academic Press.