2 research outputs found
Low-Temperature Catalytic Dry Reforming of Methane over Pd Promoted Ni–CaO–Ca<sub>12</sub>Al<sub>14</sub>O<sub>33</sub> Multifunctional Catalyst
The
dry reforming of methane (DRM) suffers from high energy consumption
and catalyst deactivation over time on stream at high operating temperatures
(>800 °C). Here, we demonstrate that DRM is effectively catalyzed
at 600 °C by Pd promoted Ni–CaO–Ca12Al14O33 multifunctional adsorbent/catalyst
materials with 67% CO2 conversion, 68% CH4 conversion,
and a H2/CO ratio close to unity. Notably, the catalyst
shows no sign of deactivation at 600 °C for a 50 h continuous
on-stream DRM reaction. The high performance is ascribed to the enhanced
CH4 dissociation activity with the presence of Pd. CH4 reformed with CaCO3 achieved the transformation
between bulk CaCO3 and nanoparticles of CaO. The dynamic
transformation may allow for reversible encapsulation and release
of Ni particles, thereby suppressing Ni sintering. Furthermore, the
coke formed on the catalyst is mainly the active carbon species which
is easily removed by CO2 and CaCO3, thus ensuring
the long-term stability. The results demonstrated herein shed light
on a new paradigm to design low-temperature DRM reaction catalysts
Morphology Effect of Ir/La<sub>2</sub>O<sub>2</sub>CO<sub>3</sub> Nanorods with Selectively Exposed {110} Facets in Catalytic Steam Reforming of Glycerol
Tuning the morphology of nanocatalysts has been regarded as a powerful
approach to high-performance heterogeneous catalysts, since the highly
active facets might be selectively exposed to reactants. Herein, we
report how the shape effect significantly improves the performance
of Ir/La<sub>2</sub>O<sub>2</sub>CO<sub>3</sub> catalyst in the steam
reforming of glycerol at high temperatures up to 650 °C toward
a sustainable hydrogen production. La<sub>2</sub>O<sub>2</sub>CO<sub>3</sub> nanorods (NRs) with different sizes and aspect ratios were
synthesized for supporting Ir nanoparticles. Compared with conventional
Ir/La<sub>2</sub>O<sub>2</sub>CO<sub>3</sub>, the NR catalysts considerably
improved the activity, selectivity, and stability, allowing for a
stable hydrogen production for 100 h without obvious deactivation.
The role of the NRs was rationalized by XRD, XPS, TPR, TPD, and HRTEM
analysis. The high performance of the NR catalyst is elucidated by
the formation of hexagonal La<sub>2</sub>O<sub>2</sub>CO<sub>3</sub> NRs with selectively exposed {110} facets under reaction conditions,
which strongly interact with Ir catalysts, thereby preventing the
tiny catalyst particles from sintering at 650 °C. A mechanistic
insight is presented to understand the interaction based on the structure
of the La<sub>2</sub>O<sub>2</sub>CO<sub>3</sub> supports
