The shift toward unconventional CO/CO2 sources
for chemicals
production is accompanied by several challenges, e.g., those associated
with their composition. The use of CO/CO2-rich steel mill
gases as an alternative feedstock promotes carbon circularity, contributing
to reducing the industry’s carbon footprint. The upgrading
of steel mill gases as a carbon source in some cases requires efficient
and selective H2 removal. This study investigates the preferential
oxidation of H2 in CO-rich streams, resembling blast furnace
steel mill gas, over a 15 wt % Ni/γ-Al2O3 catalyst combining experimental and modeling techniques. A reaction
temperature of 310 °C was selected to prevent carbonyl-induced
sintering for CO partial pressures of 26 kPa and higher. Despite the
excess CO, an O2-to-H2O selectivity of 65% was
achieved at full O2 conversion for an optimum H2/O2 inlet ratio of 3.3. By investigating the effects of
the CO and H2 inlet partial pressures, a relation between
the CO/H2 inlet ratio and the water selectivity was established.
Catalyst stability was confirmed over a 24 h oxidation test. In situ TPO showed negligible amounts of deposited carbon,
and subsequent XRD analysis showed only a minor change in diffraction
patterns. First-principles microkinetic modeling attributes the high
water selectivity over O*-saturated Ni(111) to a 33 kJ mol–1 difference in barrier between H* and CO* oxidation, which compensates
the low H*/CO* coverage ratios. The model further highlights the relation
between the CO/H2 inlet ratio and the water selectivity
with changes in the CO*/H* coverage ratio. The microkinetic model
predicts a water selectivity of 91% at 310 °C, significantly
higher than the experimental data. Combining several experimental
tests with characterization techniques, we attribute the somewhat
lower experimental selectivity to WGS activity, possible formation
of surface NiO species that are highly active for CO-PROX, and undercoordinated
Ni sites that are active for CO dissociation.