Ni@ZSM-5 catalyst prepared by direct synthesis for efficient hydrogen production through the water-gas shift reaction

A nickel-based ZSM-5 zeolite catalyst was synthesized via a one-pot approach for the hydrogen production via the water-gas shift reaction. Comprehensive characterization was performed using several complementary techniques. The presence of Ni species exhibiting different interactions with the support was evidenced by temperature-programmed reduction and near-ambient-pressure X-ray spectroscopy experiments. To compare performance, a catalyst with the same Ni loading was prepared via incipient wetness impregnation; both catalysts were active and selective for the water-gas shift reaction at 400 °C and 1 atm. Notably, the one-pot-synthesized catalyst, Ni2.4@ZSM-5, achieved higher CO conversion than the wet-impregnated catalyst, remained stable over 48 h of continuous operation (as shown by stability and on-off cycling tests), and exhibited high hydrogen selectivity. In situ DRIFT and NAP-XPS spectroscopy further revealed transient species, providing insights into the reaction mechanism.

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Publication Details

Journal
International Journal of Hydrogen Energy
Published
2026-09-11
DOI
https://doi.org/10.1016/j.ijhydene.2026.157467
Primary Topic
Catalysts for Methane Reforming
Type
article
Field-Weighted Citation Impact
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article

Ni@ZSM-5 catalyst prepared by direct synthesis for efficient hydrogen production through the water-gas shift reaction

Karim Sapag, Ana M. Tarditi, Fredy Ordoñez Ramos, Alejandra Santa-Arango et al.
International Journal of Hydrogen Energy
Catalysts for Methane Reforming
article

Ni@ZSM-5 catalyst prepared by direct synthesis for efficient hydrogen production through the water-gas shift reaction

Karim Sapag, Ana M. Tarditi, Fredy Ordoñez Ramos, Alejandra Santa-Arango, Carlos Ostos, John F. Múnera
article en

Abstract

A nickel-based ZSM-5 zeolite catalyst was synthesized via a one-pot approach for the hydrogen production via the water-gas shift reaction. Comprehensive characterization was performed using several complementary techniques. The presence of Ni species exhibiting different interactions with the support was evidenced by temperature-programmed reduction and near-ambient-pressure X-ray spectroscopy experiments. To compare performance, a catalyst with the same Ni loading was prepared via incipient wetness impregnation; both catalysts were active and selective for the water-gas shift reaction at 400 °C and 1 atm. Notably, the one-pot-synthesized catalyst, Ni2.4@ZSM-5, achieved higher CO conversion than the wet-impregnated catalyst, remained stable over 48 h of continuous operation (as shown by stability and on-off cycling tests), and exhibited high hydrogen selectivity. In situ DRIFT and NAP-XPS spectroscopy further revealed transient species, providing insights into the reaction mechanism.

International Journal of Hydrogen EnergyVol. 275
Universidad Nacional del Litoral (AR), Universidad de Antioquia (CO), National University of San Luis (AR)
Consejo Nacional de Investigaciones Científicas y Técnicas
Clean water and sanitation
Openalex Percentile: Top 30%
Catalysts for Methane Reforming
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Ni@ZSM-5 catalyst prepared by direct synthesis for efficient hydrogen production through the water-gas shift reaction — Karim Sapag, Ana M. Tarditi, et al. · International Journal of Hydrogen Energy (2026) | TGRS Research Map | TGRS