Hydroprocessing catalysts were prepared using fibrillar alumina and at
tapulgite as carrier materials and nickel and molybdenum as active sub
stances. With fibrillar alumina as primary particles, a carrier materi
al was obtained which combined a large surface area (138 m(2)/g) with
a large average pore diameter (252 Angstrom). Due to side-by-side asso
ciation of the fibers, attapulgite did not yield a catalyst carrier wi
th as large pores as was expected. The catalysts were tested for hydro
processing of an atmospheric petroleum resid, and the results were com
pared with those obtained for a commercial catalyst with similar loadi
ng of nickel and molybdenum. The catalyst prepared using fibrillar alu
mina as carrier material was more active than the commercial catalyst
for hydrodemetalization, equally active for hydrodesulfurization, and
less active for hydrodenitrogenation. The catalyst prepared using atta
pulgite as carrier material was inferior to the other two catalysts in
all respects.