S. Morin et al., INFLUENCE OF COKE DEPOSITS ON THE SELECTIVITY OF M-XYLENE TRANSFORMATION AND ON THE ISOMERIZATION MECHANISM, Applied catalysis. A, General, 168(1), 1998, pp. 63-68
m-Xylene transformation was carried out at 623 K over a series of comm
ercial HFAU zeolites with framework Si/Al ratios between 4 and 100. Al
l the samples deactivate rapidly owing to the formation of coke. The l
ower the Si/Al ratio the faster the deactivation, which can be explain
ed by the increase in acid strength when the Si/Al ratio decreases and
by the faster deactivation of the strong acid sites shown by the effe
ct of cake on the intensity of the various OH IR bands. Deactivation c
auses a significant increase in the disproportionation/isomerization r
ate ratio (D/I) and a significant decrease in the para/ortho selectivi
ty (p/o). These selectivity changes can be related to a greater select
ivity of the strong acid sites in favor of the classical monomolecular
mode of isomerization at the expense of disproportionation and of the
bimolecular mode of isomerization (through m-xylene disproportionatio
n followed by m-xylene-trimethylbenzenes transalkylation). This was co
nfirmed by the fact that pyridine poisoning and deactivation by coke d
eposition have an identical effect on D/I and p/o selectivities. The r
apid transformation into coke of the diphenylmethane intermediates of
disproportionation and of bimolecular isomerization on the strong acid
sites was proposed in order to explain the low selectivity of these s
ites for these reactions. (C) 1998 Elsevier Science B.V.