Unveiling the role of Ni nanometric particles in ultra-stable hierarchically porous Y zeolite to drive methane steam reforming and CO2 hydrogenation

Three catalysts containing 5, 10 and 20 % wt. Ni trapped in the porous zeolite framework (Ni5, Ni10 and Ni20, respectively), were prepared. An ultra-stable zeolite Y, with a Si/Al molar ratio of 385, selected for its high thermal stability, was impregnated under vacuum with an aqueous solution of Ni 2+ ions and thermally treated at 600 °C in a reducing atmosphere. The Ni nominal contents were compliant with the nominal value as confirmed by X-ray fluorescence spectroscopy. The catalysts were tested in the steam reforming of methane and in the hydrogenation of carbon dioxide. Catalytic activity is significantly structure-dependant. Several physical-chemical characterizations were carried out. X-ray powder diffraction with synchrotron source, followed by Rietveld analysis, and H 2 -TPR analysis indicate that all the loaded nickel is in the metallic form. High-resolution transmission electron microscopy showed that the particle size distribution is centred around 30 nm for Ni5 and Ni 10, while particles of around 150 nm are obtained with Ni20. A thorough NLDFT analysis of the pore size distribution shows a certain fraction of large mesoporosity in addition to the microporosity typical of zeolites. This hierarchical structure, also evidenced by the TEM micrographs, has a profound impact on the catalytic response since the nickel particles are located in the mesoporosity, whereas the reaction appears limited by Knudsen diffusion through zeolite micropores. O 2 -TPOs carried out on used samples showed no coke deposition suggesting a good resistance to fouling, that can be related to a very low acidity, as measured by NH 3 -TPD measurements. • Ni nanoparticles (5–20 wt%) were supported onto USY zeolite with Si/Al = 385. • Catalysts are active towards methane steam reforming and CO 2 hydrogenation. • USY exhibits hierarchical porosity with micro- and mesopores (hosting Ni NPs). • Internal mass transfer limitations occur due to Knudsen diffusion inside micropores. • Reactions are structure-sensitive; activity and selectivity depend on Ni particle size.

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Publication Details

Journal
International Journal of Hydrogen Energy
Published
2025-01-22
DOI
https://doi.org/10.1016/j.ijhydene.2025.01.244
Citations
3
Primary Topic
Catalysts for Methane Reforming
Type
article
Field-Weighted Citation Impact
1.17

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article

Unveiling the role of Ni nanometric particles in ultra-stable hierarchically porous Y zeolite to drive methane steam reforming and CO2 hydrogenation

Anna Basco, Serena Esposito, Antonello Marocco, Michele Pansini et al.
3 citations
International Journal of Hydrogen Energy
Catalysts for Methane Reforming
1.17
article

Unveiling the role of Ni nanometric particles in ultra-stable hierarchically porous Y zeolite to drive methane steam reforming and CO2 hydrogenation

Anna Basco, Serena Esposito, Antonello Marocco, Michele Pansini, Rossella Arletti, Olimpia Tammaro, Gianluca Landi, Giulia Sorbino, Mattia Sisti, Alessandro Padua, Stefano Scognamiglio
article en
3 citations

Abstract

Three catalysts containing 5, 10 and 20 % wt. Ni trapped in the porous zeolite framework (Ni5, Ni10 and Ni20, respectively), were prepared. An ultra-stable zeolite Y, with a Si/Al molar ratio of 385, selected for its high thermal stability, was impregnated under vacuum with an aqueous solution of Ni 2+ ions and thermally treated at 600 °C in a reducing atmosphere. The Ni nominal contents were compliant with the nominal value as confirmed by X-ray fluorescence spectroscopy. The catalysts were tested in the steam reforming of methane and in the hydrogenation of carbon dioxide. Catalytic activity is significantly structure-dependant. Several physical-chemical characterizations were carried out. X-ray powder diffraction with synchrotron source, followed by Rietveld analysis, and H 2 -TPR analysis indicate that all the loaded nickel is in the metallic form. High-resolution transmission electron microscopy showed that the particle size distribution is centred around 30 nm for Ni5 and Ni 10, while particles of around 150 nm are obtained with Ni20. A thorough NLDFT analysis of the pore size distribution shows a certain fraction of large mesoporosity in addition to the microporosity typical of zeolites. This hierarchical structure, also evidenced by the TEM micrographs, has a profound impact on the catalytic response since the nickel particles are located in the mesoporosity, whereas the reaction appears limited by Knudsen diffusion through zeolite micropores. O 2 -TPOs carried out on used samples showed no coke deposition suggesting a good resistance to fouling, that can be related to a very low acidity, as measured by NH 3 -TPD measurements. • Ni nanoparticles (5–20 wt%) were supported onto USY zeolite with Si/Al = 385. • Catalysts are active towards methane steam reforming and CO 2 hydrogenation. • USY exhibits hierarchical porosity with micro- and mesopores (hosting Ni NPs). • Internal mass transfer limitations occur due to Knudsen diffusion inside micropores. • Reactions are structure-sensitive; activity and selectivity depend on Ni particle size.

International Journal of Hydrogen EnergyVol. 103
University of Modena and Reggio Emilia (IT), Politecnico di Torino (IT), Università degli studi di Cassino e del Lazio Meridionale (IT), National Interuniversity Consortium of Materials Science and Technology (IT)
Ministero della transizione ecologica, Ministero dell'Università e della Ricerca
Openalex Percentile: Top 25%
Catalysts for Methane Reforming
1.17
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