Biomass
gasification is a sustainable way to convert biomass residues
into valuable fuels and chemicals via syngas production. However,
several gas impurities need to be removed before the final synthesis.
Understanding of the interactions and effects of biomass-derived producer
gas contaminants (S and K) on the performance of reforming catalysts
is of great importance when it comes to process reliability and development.
In the present study, the steam reforming activity at 800 °C
of a sulfur-equilibrated nickel catalyst during controlled exposure
to alkali species (∼2 ppmv K) and in its absence was investigated
using real producer gas from a 5 kWth O2-blown
fluidized-bed gasifier. Conversions of CH4, C2H4, and C10H8 were used to evaluate
the performance of the Ni/MgAl2O4 catalyst and
MgAl2O4 support. A significant and positive
effect on the catalyst activity is observed with addition of gas-phase
KCl. This is assigned primarily to the observed K-induced reduction
in sulfur coverage (θS) on Nian effect which
is reversible. The catalytic contribution of the K-modified pure MgAl2O4 support was found to be significant in the conversion
of naphthalene but not for light hydrocarbons. The product and catalyst
analyses provided evidence to elucidate the preferential adsorption
site for S and K on the catalyst as well as the role of the support.
Whereas S, as expected, was found to preferentially adsorb on the
surface of Ni particles, forming S-Ni sites, K was found to preferentially
adsorb on the MgAl2O4 support. A low but still
significant K adsorption on S–Ni sites, or an effect on only
the fraction of exposed Ni surface area near the metal–support
interface, can, however, not be excluded. The result suggests that
an improved Ni/MgAl2O4 catalyst activity and
an essentially carbon-free operation can be achieved in the presence
of controlled amount of gas-phase potassium and high sulfur coverages
on Ni. Based on the results, a mechanism of the possible K–S
interactions is proposed.