T. Isoda et al., REACTIVITY AND SELECTIVITY FOR THE HYDROCRACKING OF VACUUM GAS OIL OVER METAL-LOADED AND DEALUMINATED Y-ZEOLITES, Energy & fuels, 12(3), 1998, pp. 493-502
Hydrocracking, hydrodenitrogenation (HDN), and hydrodesulfurization (H
DS) of vacuum gas oil (VGO) were examined using Ni-, Co-, and Fe-loade
d and dealuminated Y-zeolites at 300-380 degrees C under an initial hy
drogen pressure of 5 MPa. The major fraction of the VGO was n-paraffin
s (45 wt %), and the second major fraction was alkyl-substituted 3- an
d 4-ring aromatics. Polar aromatics and 1- and 2-ring aromatics were m
inor components. Paraffins of 15-32 carbon chains and aromatic compoun
ds of 3-4 rings were efficiently hydrocracked into a gasoline fraction
over Ni-HY-A (Si/2Al = 16.0) zeolite, which gave the least yield of g
aseous byproducts among the catalysts examined. Extensively dealuminat
ed Ni-HY-B zeolite (Si/2Al = 50.0) produced a large amount of middle d
istillate fraction, while the yields of gas and coke that was deposite
d on the catalyst were markedly suppressed. Both zeolites exhibited ex
cellent HDN and HDS activities. The Co-HY and Fe-HY zeolites showed a
similar hydrocracking activity as did the Ni-HY-A zeolite, whereas the
Fe-HY produced more gaseous hydrocarbons. The Co-HY and Fe-HY zeolite
s were inferior to the Ni-HY-A in HDS and HDN activities at 380 degree
s C. The metal-free HY-A zeolite exhibited higher yields of gaseous hy
drocarbons, 4-ring aromatics, coke, and hexane-insoluble fractions tha
n did the metal-loaded catalysts. The HY-A zeolite had essentially no
HDS and HDN activities, and the concentration of alkyldibenzothiophene
s in the product oil was increased by condensation and transalkylation
during cracking reaction. The excellent activities of the metal-loade
d HY-zeolites apparently originated from the optimized acidity, as a r
esult of dealumination, in addition to the highly dispersed metal sulf
ides which enhanced hydrogenation activity. The acidic strength of the
catalysts was a key factor in controlling the selectivity between gas
oline and gas oil production.