The conversion of,l-hexane and 2,2,4 triMe-pentane was studied at 723 K on
a USY-zeolite (Si/Al: frame=30; bulk=2.7) in an electrobalance reactor with
external recirculation. The influence of the coke content on the reaction
paths involved in the conversion of paraffinic model components was evaluat
ed. Coke formation from propylene and i-butene, the main olefinic products
formed during the conversion of the two paraffinic model components, was in
vestigated.
Under the conditions used, an increase in the molar WC ratio of the product
s as a function of coke yield can be observed due to hydride transfer react
ions with coke. Coke molecules cannot be considered as being inert with res
pect to the cracking reactions and their formation leads to the occurrence
of reactions that can strongly influence the catalyst performance. In parti
cular, the potential of coke molecules to form highly delocalized carbenium
ions and their ability to act as hydride donor towards surface carbenium i
ons provides reaction paths to paraffinic reaction products.
The effect of coke is not identical for all the elementary reactions involv
ed in the conversion of the paraffinic model components. (C) 2000 Elsevier
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