Enhanced coking resistance in methane dry reforming using anti-sintering Ni nanoparticles and atomically re-dispersed oxygen vacancy-rich CeOx on MgAl2O4 support

The dry reforming of methane (DRM) with carbon dioxide offers a sustainable approach for producing valuable syngas (H 2 + CO); however, its industrial implementation remains constrained by the challenge of developing robust catalysts capable of efficiently cracking C–H bonds and activating C O bonds. In this study, we demonstrate that precise control over the geometric exposure and chemical states of Ni and Ce species on MgAl 2 O 4 support significantly enhances DRM performance and stability under relevant conditions, with no observed sintering or coke formation. Through a combination of catalyst testing and detailed characterization—including HAADF/STEM-EDX, H 2 -XRD, H 2 -XPS, H 2 -TPR, and CO 2 -TPD analyses —we reveal a regioselective reconstruction of MgAl 2 O 4 cross-border crystallites with CeO x atoms or clusters after reduction in H 2 flow or exposure to the DRM reaction at 750 °C. These atomically re-dispersed CeO x sites on MgAl 2 O 4 , along with residual non-stoichiometric NiAl 2 O x , act as oxygen vacancy sinks, promoting further CO 2 activation, while anti-sintering Ni particles (sub-7.5 nm) efficiently crack CH 4 . This synergistic catalysis between Ni and CeO x species effectively suppresses coke accumulation, ensuring prolonged stability of the Ni x /Ce-MA catalysts. Notably, a Ni (2 wt%)-based CeO x (5 wt%)-MgAl 2 O 4 catalyst achieved stable syngas production with an H 2 /CO molar ratio of ∼0.76–0.93 at 750 °C for up to 100 h on-stream. This study provides valuable insights into the design of more efficient DRM catalysts and underscores the potential of multivalent oxides for enhancing atom economy in catalysis. • Tailored Ni and Ce exposure and states improve catalytic efficiency in methane dry reforming. • Highly reactive, anti-sintering sub-7.5 nm Ni particles promote effective CH 4 decomposition. • Atomically re-dispersed CeO x on MgAl 2 O 4 interfaces act as oxygen vacancy sinks, aiding CO 2 activation. • Ni and Ce δ+ redox species interact synergistically to suppress coke formation effectively.

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Publication Details

Journal
Materials Today Chemistry
Published
2025-04-01
DOI
https://doi.org/10.1016/j.mtchem.2025.102673
Citations
6
Primary Topic
Catalysts for Methane Reforming
Type
article
Field-Weighted Citation Impact
2.33
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article

Enhanced coking resistance in methane dry reforming using anti-sintering Ni nanoparticles and atomically re-dispersed oxygen vacancy-rich CeOx on MgAl2O4 support

M. El Doukkali
6 citations
Materials Today Chemistry
Catalysts for Methane Reforming
2.33
article

Enhanced coking resistance in methane dry reforming using anti-sintering Ni nanoparticles and atomically re-dispersed oxygen vacancy-rich CeOx on MgAl2O4 support

M. El Doukkali
article en
6 citations

Abstract

The dry reforming of methane (DRM) with carbon dioxide offers a sustainable approach for producing valuable syngas (H 2 + CO); however, its industrial implementation remains constrained by the challenge of developing robust catalysts capable of efficiently cracking C–H bonds and activating C O bonds. In this study, we demonstrate that precise control over the geometric exposure and chemical states of Ni and Ce species on MgAl 2 O 4 support significantly enhances DRM performance and stability under relevant conditions, with no observed sintering or coke formation. Through a combination of catalyst testing and detailed characterization—including HAADF/STEM-EDX, H 2 -XRD, H 2 -XPS, H 2 -TPR, and CO 2 -TPD analyses —we reveal a regioselective reconstruction of MgAl 2 O 4 cross-border crystallites with CeO x atoms or clusters after reduction in H 2 flow or exposure to the DRM reaction at 750 °C. These atomically re-dispersed CeO x sites on MgAl 2 O 4 , along with residual non-stoichiometric NiAl 2 O x , act as oxygen vacancy sinks, promoting further CO 2 activation, while anti-sintering Ni particles (sub-7.5 nm) efficiently crack CH 4 . This synergistic catalysis between Ni and CeO x species effectively suppresses coke accumulation, ensuring prolonged stability of the Ni x /Ce-MA catalysts. Notably, a Ni (2 wt%)-based CeO x (5 wt%)-MgAl 2 O 4 catalyst achieved stable syngas production with an H 2 /CO molar ratio of ∼0.76–0.93 at 750 °C for up to 100 h on-stream. This study provides valuable insights into the design of more efficient DRM catalysts and underscores the potential of multivalent oxides for enhancing atom economy in catalysis. • Tailored Ni and Ce exposure and states improve catalytic efficiency in methane dry reforming. • Highly reactive, anti-sintering sub-7.5 nm Ni particles promote effective CH 4 decomposition. • Atomically re-dispersed CeO x on MgAl 2 O 4 interfaces act as oxygen vacancy sinks, aiding CO 2 activation. • Ni and Ce δ+ redox species interact synergistically to suppress coke formation effectively.

Materials Today ChemistryVol. 45
Centre National de la Recherche Scientifique (FR), Dalian Institute of Chemical Physics (CN), Chinese Academy of Sciences (CN), Université de Lille (FR), Université Sultan Moulay Slimane (MA), Unité de catalyse et de chimie du solide de Lille (FR), Université d'Artois (FR), École Centrale de Lille (FR)
Openalex Percentile: Top 12%
Catalysts for Methane Reforming
2.33
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