The effect of pretreatment, using hydrogen or carbon monoxide, on the activ
ity and selectivity of a ruthenium promoted cobalt catalyst (Ru(0.20 wt%)/C
o(10 wt%)TiO2) during Fischer-Tropsch (FT) synthesis was studied in a conti
nuous-stirred tank reactor (CSTR). The hydrogen reduced catalyst exhibited
a high initial synthesis gas conversion (72.5%) and reached steady stale af
ter 40 h on stream, after which the catalyst deactivated slightly with time
on stream. The carbon monoxide reduced catalyst reached steady state quick
ly and showed a lower activity and a good stability. Methane selectivity on
the carbon monoxide reduced catalyst was 15-20% (carbon base), much higher
than that on the hydrogen reduced catalyst (5-10%). Carbon monoxide regene
ration increased the activity on the hydrogen reduced catalyst; however, it
did not have significant effect on the carbon monoxide reduced catalyst.