Cu and Cu/ZnO Carbon-Based Catalysts for the Water-Gas Shift Reaction

In this work, water-gas shift reaction is studied using Cu/ZnO catalysts supported on activated carbons derived from residual olive stone, obtained by physical activation with steam or CO 2 . The steam-activated support, ACH 2 O, exhibits high surface area and broad pore size distribution, which facilitates Cu dispersion. This catalyst displays very high catalytic activity, without the need to incorporate ZnO, showing X CO = 80 %, full selectivity to H 2 , and a promising hydrogen productivity of 120 μmol·(g Cu-ICP ·s) −1 at 300 °C. The CO 2 -activated support shows a lower surface area, mainly dominated by micropores, yielding a lower Cu dispersion. The addition of ZnO enhances Cu dispersion and its catalytic activity, but it remains lower than that of Cu-ACH 2 O. These results are slightly better than those obtained by a commercial catalyst, Cu/ZnO, suggesting that an adequate design of the porosity support can avoid the need for ZnO as promoter, even using a more renewable and sustainable synthesis pathway.

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Publication Details

Journal
International Journal of Hydrogen Energy
Published
2026-11-11
DOI
https://doi.org/10.1016/j.ijhydene.2026.158622
Primary Topic
Catalysts for Methane Reforming
Type
article
Field-Weighted Citation Impact
0.00

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article

Cu and Cu/ZnO Carbon-Based Catalysts for the Water-Gas Shift Reaction

Juana María Rosas, T. Cordero, Diego Cazorla‐Amorós, J. Rodríguez‐Mirasol et al.
International Journal of Hydrogen Energy
Catalysts for Methane Reforming
article

Cu and Cu/ZnO Carbon-Based Catalysts for the Water-Gas Shift Reaction

Juana María Rosas, T. Cordero, Diego Cazorla‐Amorós, J. Rodríguez‐Mirasol, M.N. Rivas-Márquez, R. Ruiz-Rosas, M. Navlani-García, P. Riquelme-García
article en

Abstract

In this work, water-gas shift reaction is studied using Cu/ZnO catalysts supported on activated carbons derived from residual olive stone, obtained by physical activation with steam or CO 2 . The steam-activated support, ACH 2 O, exhibits high surface area and broad pore size distribution, which facilitates Cu dispersion. This catalyst displays very high catalytic activity, without the need to incorporate ZnO, showing X CO = 80 %, full selectivity to H 2 , and a promising hydrogen productivity of 120 μmol·(g Cu-ICP ·s) −1 at 300 °C. The CO 2 -activated support shows a lower surface area, mainly dominated by micropores, yielding a lower Cu dispersion. The addition of ZnO enhances Cu dispersion and its catalytic activity, but it remains lower than that of Cu-ACH 2 O. These results are slightly better than those obtained by a commercial catalyst, Cu/ZnO, suggesting that an adequate design of the porosity support can avoid the need for ZnO as promoter, even using a more renewable and sustainable synthesis pathway.

International Journal of Hydrogen EnergyVol. 292
University of Alicante (ES), Universidad de Málaga (ES)
Universidad de Málaga, Ministerio de Ciencia, Innovación y Universidades, Junta de Andalucía
Affordable and clean energy
Catalysts for Methane Reforming
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