The activity and selectivity of iron-based slurry-phase catalysts were
investigated for the hydrogenation of pyrene and the hydrocracking of
C-C bonds in several model compounds: 1-methylnaphthalene (1-MN), 2-h
exylnaphthalene (2-HN) and 4-(1-naphthylmethyl)bibenzyl (NMBB). Reacti
ons were performed under typical coal liquefaction conditions. Higher
reaction temperature and the presence of sulfur increased the hydrogen
ation of pyrene by the iron catalysts generated in situ. The in situ m
ethod of catalyst addition was most effective for pyrene hydrogenation
for the. iron catalysts, while molybdenum naphthenate showed increase
d activity with two-stage processing. Both Fe and Mo catalysts showed
low activity in reactions where the catalyst was generated ex situ. Co
mbinations of Fe and Mo catalysts were synergistic for pyrene hydrogen
ation, although the amount of increase was dependent upon the particul
ar iron precursor used. The Fe and Mo catalysts affected the hydrocrac
king of the three model species differently. Molybdenum naphthenate wa
s more active for hydrocracking 2-HN and NMBB than any of the Fe catal
ysts, but combining FeNaph with MoNaph was detrimental to the hydrocra
cking of these compounds. The selectivity of hydrocracking NMBB at spe
cific bonding sites was affected by the presence and type of catalyst,
presence of sulfur, and reaction time.