2 research outputs found
CO<sub>2</sub> Activation over Nanoshaped CeO<sub>2</sub> Decorated with Nickel for Low-Temperature Methane Dry Reforming
Dry reforming of methane (DRM) is a promising way to
convert methane
and carbon dioxide into H2 and CO (syngas). CeO2 nanorods, nanocubes, and nanospheres were decorated with 1–4
wt % Ni. The materials were structurally characterized using TEM and in situ XANES/EXAFS. The CO2 activation was analyzed
by DFT and temperature-programmed techniques combined with MS-DRIFTS.
Synthesized CeO2 morphologies expose {111} and {100} terminating
facets, varying the strength of the CO2 interaction and
redox properties, which influence the CO2 activation. Temperature-programmed
CO2 DRIFTS analysis revealed that under hydrogen-lean conditions
mono- and bidentate carbonates are hydrogenated to formate intermediates,
which decompose to H2O and CO. In excess hydrogen, methane
is the preferred reaction product. The CeO2 cubes favor
the formation of a polydentate carbonate species, which is an inert
spectator during DRM at 500 °C. Polydentate covers a considerable
fraction of ceria’s surface, resulting in less-abundant surface
sites for CO2 dissociation
Effects of Zr Doping into Ceria for the Dry Reforming of Methane over Ni/CeZrO<sub>2</sub> Catalysts: In Situ Studies with XRD, XAFS, and AP-XPS
The
methane activation and methane dry reforming reactions were
studied and compared over 4 wt % Ni/CeO2 and 4 wt % Ni/CeZrO2 (containing 20 wt % Zr) catalysts. Upon the incorporation
of Zr into the ceria support, the catalyst exhibited a significantly
improved activity and H2 selectivity. To understand the
effects of the Zr dopant on Ni and CeO2 during the dry
reforming of methane (DRM) reaction and to probe the structure–reactivity
relationship underlying the enhanced catalytic performance of the
mixed-oxide system, in situ time-resolved X-ray diffraction (TR-XRD),
X-ray absorption fine structure (XAFS), and ambient-pressure X-ray
photoelectron spectroscopy (AP-XPS) were employed to characterize
the catalysts under reaction conditions. TR-XRD and AP-XPS indicate
that ceria–zirconia supported Ni (Ni/CeZrO2) is
of higher reducibility than the pure ceria supported Ni (Ni/CeO2) upon the reaction with pure CH4 or for the methane
dry reforming reaction. The active state of Ni/CeZrO2 under
optimum DRM conditions (700 °C) was identified as Ni0, Ce3+/Ce4+, and Zr4+. The particle
size of both nickel and the ceria support under reaction conditions
was analyzed by Rietveld refinement and extended XAFS fitting. Zr
in the ceria support prevents particle sintering and maintains small
particle sizes for both metallic nickel and the partially reduced
ceria support under reaction conditions through a stronger metal–support
interaction. Additionally, Zr prevents Ni migration from the surface
into ceria forming a Ce1–xNixO2–y solid
solution, which is seen in Ni/CeO2, thus helping to preserve
the active Ni0 on the Ni/CeZrO2 surface
