Reuse of CO-Oxidation Spent Catalysts for Dry Reforming of Methane: Techno-Economic Analysis

We report an upcycling route for Pt-based spent CO-oxidation catalysts in stationary plants. By simple Ni impregnation, the spent modules are converted into active dry reforming of methane (DRM) catalysts (oxiCO/Ni). Under DRM at 750 °C, oxiCO/Ni achieves CH4 and CO2 conversions >73 and >94%, respectively, with high structural and thermal stability maintained over 7 h of continuous operation. The superior activity and resistance to deactivation are attributed to the formation of the NiAl2O4 spinel phase, strong metal–support interactions, and synergistic effects from residual Pt and La in the spent catalyst. A techno-economic analysis was conducted for a recycling plant capable of processing 205 tons/y of raw spent oxiCO catalyst modules, yielding 16.2 tons/y of oxiCO/Ni catalyst for DRM. The profitability analysis showed that the investment in such a project is profitable with a maximum tipping credit of 6500 US$/ton, giving a net present value of US$ 6.9 million, an internal rate of return of 43%, and a discounted payback time of 4 years and 1 month. This approach couples waste minimization with catalyst circularity, delivering both environmental and economic benefits.

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Publication Details

Journal
ACS Sustainable Chemistry & Engineering
Published
2026-01-12
DOI
https://doi.org/10.1021/acssuschemeng.5c09652
Primary Topic
Catalysts for Methane Reforming
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article
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article

Reuse of CO-Oxidation Spent Catalysts for Dry Reforming of Methane: Techno-Economic Analysis

Nada Abounahia, Ahmed Abotaleb, Alessandro Sinopoli, Francesco Ferella
ACS Sustainable Chemistry & Engineering
Catalysts for Methane Reforming
article

Reuse of CO-Oxidation Spent Catalysts for Dry Reforming of Methane: Techno-Economic Analysis

Nada Abounahia, Ahmed Abotaleb, Alessandro Sinopoli, Francesco Ferella
article en

Abstract

We report an upcycling route for Pt-based spent CO-oxidation catalysts in stationary plants. By simple Ni impregnation, the spent modules are converted into active dry reforming of methane (DRM) catalysts (oxiCO/Ni). Under DRM at 750 °C, oxiCO/Ni achieves CH4 and CO2 conversions >73 and >94%, respectively, with high structural and thermal stability maintained over 7 h of continuous operation. The superior activity and resistance to deactivation are attributed to the formation of the NiAl2O4 spinel phase, strong metal–support interactions, and synergistic effects from residual Pt and La in the spent catalyst. A techno-economic analysis was conducted for a recycling plant capable of processing 205 tons/y of raw spent oxiCO catalyst modules, yielding 16.2 tons/y of oxiCO/Ni catalyst for DRM. The profitability analysis showed that the investment in such a project is profitable with a maximum tipping credit of 6500 US$/ton, giving a net present value of US$ 6.9 million, an internal rate of return of 43%, and a discounted payback time of 4 years and 1 month. This approach couples waste minimization with catalyst circularity, delivering both environmental and economic benefits.

ACS Sustainable Chemistry & EngineeringVol. 14(3)
University of Messina (IT), University of L'Aquila (IT), Hamad bin Khalifa University (QA), Qatar Foundation (QA)
Openalex Percentile: Top 91%
Catalysts for Methane Reforming
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Reuse of CO-Oxidation Spent Catalysts for Dry Reforming of Methane: Techno-Economic Analysis — Nada Abounahia, Ahmed Abotaleb, et al. · ACS Sustainable Chemistry & Engineering (2026) | TGRS Research Map | TGRS