Abstract:Based on the characteristics
of typical C9
+ aromatics in naphtha fractions,
the effects of key process parameters
and heavy aromatic composition on product distribution of fluid catalytic
cracking (FCC) of heavy aromatics (HAs) were investigated. The results
show that catalysts with large pore size and strong acid sites are
favorable for the conversion of HAs to benzene–toluene–xylene
(BTX) at higher reaction temperatures and moderate catalyst–oil
ratios (C/O). With a Y zeolite-based catalyst which was hydrot… Show more
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