Abstract
A moderately acidic ferrisilicate zeolite of the pentasil type has been used to promote the support acidity of both mono- and bimetallic naphtha reforming catalyst formulations. The added zeolite (1-10 wt.%) enhances the number of isomerization sites and also catalyses the oligomerization of the cracked products into aromatics. The oligomerization activity is maximal when the reaction is carried out with recycling of gaseous products.
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