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Highly Efficient and Stable Methane Dry Reforming Enabled by a Single-Site Cationic Ni Catalyst
Qingpeng Cheng1,2, Xueli Yao2, Lifeng Ou3
1Physical Sciences and Engineering Division, Advanced Membranes and Porous Materials (AMPM) Center, King Abdullah University of Science and Technology (KAUST), Thuwal 23955-6900, Saudi Arabia.
Zeolite-supported nickel catalysts show enhanced activity and stability in methane dry reforming. Cationic nickel sites within the MFI zeolite framework enable a unique reaction pathway, preventing coke formation and improving catalyst design.
Area of Science:
- Catalysis
- Materials Science
- Chemical Engineering
Background:
- Zeolite-supported nickel (Ni) catalysts are crucial for methane dry reforming (DRM).
- Typically, Ni is reduced to its metallic state to function as the active site.
- Understanding Ni's role in zeolite frameworks is key to improving catalyst performance.
Purpose of the Study:
- To investigate the catalytic behavior of Ni incorporated into the MFI zeolite framework for DRM.
- To elucidate the reaction mechanism of cationic Ni sites in comparison to metallic Ni.
- To develop more stable and active Ni-based catalysts for DRM.
Main Methods:
- Ligand-protected synthesis for high Ni incorporation into MFI zeolite.
- Dry reforming of methane (DRM) reaction at 600 °C.
- Theoretical calculations and experimental validation of reaction intermediates.
Main Results:
- Ni incorporated into the MFI zeolite framework retained its cationic state during DRM.
- Cationic Ni sites exhibited higher apparent catalytic activity and stability than metallic Ni.
- Formation of metal-oxygen (Niδ+-O(2-ξ)-) pairs as active sites was identified.
Conclusions:
- Cationic Ni-MFI catalysts promote methane C-H bond dissociation via a unique mechanism.
- The CH oxidation pathway on cationic Ni sites inhibits coke formation.
- These findings guide the design of advanced Ni-based DRM catalysts.
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