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.
Authors
- Anna Basco
- Serena Esposito (ORCID: https://orcid.org/0000-0001-9159-0541)
- Antonello Marocco (ORCID: https://orcid.org/0000-0001-6628-8463)
- Michele Pansini (ORCID: https://orcid.org/0000-0001-5084-7013)
- Rossella Arletti (ORCID: https://orcid.org/0000-0001-9878-8657)
- Olimpia Tammaro (ORCID: https://orcid.org/0000-0002-4226-8801)
- Gianluca Landi (ORCID: https://orcid.org/0000-0003-4978-6465)
- Giulia Sorbino
- Mattia Sisti (ORCID: https://orcid.org/0009-0006-5402-2784)
- Alessandro Padua
- Stefano Scognamiglio
Institutions
- 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)
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
Funders
- Ministero della transizione ecologica
- Ministero dell'Università e della Ricerca