A large-pore hydrodemetallation catalyst was treated with anthracene (
AN) or a bitumen feed (BIT) in mineral oil solvent to obtain coke leve
ls up to 12% carbon. In some runs, carbazole was added to the AN-cokin
g run and in others, a nickel porphyrin compound was added to the BIT-
coking run. Physical properties of the coked catalysts were determined
, as well as catalyst activities for hydrogenation (HYD) and for hydro
denitrogenation (HDN) using a mixture of naphthalene and indole in n-h
eptane. It was found that the coke produced via BIT appeared to be por
ous, while that from AN was non-porous. A significant enhancement in n
itrogen on the catalyst over that in the bitumen feed was observed. Ca
talytic activities of the coked catalysts decreased with increasing co
ke content, with HDN activity loss being greater than HYD activity. Ne
ither the nature of the coke precursor, nor the presence of nitrogen o
r nickel on the catalyst, affected the extent of deactivation. Apparen
t activation energies decreased with increasing coke content. The role
of coke on catalyst deactivation is discussed in terms of its effect
on the distribution of different catalytically active sites for the re
actions.