The hydrocracking reaction pathways and kinetics of alkyl aromatic str
uctural elements present in typical petroleum feedstocks were probed t
hrough experiments at 350 degrees C and 1000 psig of hydrogen pressure
with a Shell NiW/USY zeolite catalyst. Experimental results for C4-C1
5 alkylbenzenes provided insight into their respective alkane-like and
aromatic-like character, as well as the effect of side-chain length o
n the kinetics and product selectivities. Initial product selectivitie
s indicated that the expected prototypical ring dealkylation to benzen
e was accompanied by other significant reactions. Reactions in the sid
e chain produced various shorter-chain alkylbenzenes, including toluen
e. Ring closure of the side chain was also significant, producing hydr
oaromatic bicyclic compounds. The overall reaction rate was first orde
r and generally increased with increasing alkyl side-chain length.