Development and Evaluation of Ni–Cu–Pt Monolithic Catalysts for Improved Ethanol Autothermal Reforming and Hydrogen Production

This study investigates the development and characterization of Ni-based catalytic monoliths for ethanol reforming, focusing on the effects of incorporating Cu and Pt as promoters. Al2O3 monoliths were coated with α-Al2O3 and impregnated with Ni, Cu, and Pt by using a wet impregnation method. The catalysts were characterized by field-emission scanning electron microscopy (FESEM), energy-dispersive spectroscopy (EDS), X-ray diffraction (XRD), X-ray photoelectron spectroscopy (XPS), and temperature-programmed reduction (TPR). The multitechnique characterization results revealed differences between the monometallic Ni/α-Al2O3 catalyst and the trimetallic Ni-Cu-Pt/α-Al2O3 catalyst. A unique flower-like structure was identified in the trimetallic catalyst, formed due to acid leaching during the Pt impregnation step. The metal impregnation process did not alter the crystalline structure of the Al2O3 substrate with both catalysts primarily exhibiting oxide phases. The Ni-Cu-Pt/α-Al2O3 catalyst has surface concentrations of Cu and Pt around 1.3% or lower, while Ni concentration exceeds 4.8%, confirming the presence of all three metals at the catalyst surface, despite the acid leaching caused by the Pt impregnation. TPR analysis indicated complex metal-support interactions in the trimetallic catalyst, with distinct reduction peaks compared with the monometallic Ni/α-Al2O3 catalyst. Catalytic evaluation revealed that the trimetallic catalyst achieved similar ethanol conversion in comparison with the monometallic Ni/α-Al2O3 catalyst but exhibited lower hydrogen selectivity due to reduced C–C bond breaking, likely influenced by the presence of Cu. These findings highlight the potential and challenges of using trimetallic catalysts in ethanol reforming, with implications for optimizing catalyst composition and reaction conditions for hydrogen production.

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Publication Details

Journal
Energy & Fuels
Published
2024-11-12
DOI
https://doi.org/10.1021/acs.energyfuels.4c04113
Citations
5
Primary Topic
Catalysts for Methane Reforming
Type
article
Field-Weighted Citation Impact
0.53

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article

Development and Evaluation of Ni–Cu–Pt Monolithic Catalysts for Improved Ethanol Autothermal Reforming and Hydrogen Production

Bruno L. D. Santos, W. A. A. Macedo, Camilla D. M. Nickel, Jéssica Florinda Zeitoune et al.
5 citations
Energy & Fuels
Catalysts for Methane Reforming
0.53
article

Development and Evaluation of Ni–Cu–Pt Monolithic Catalysts for Improved Ethanol Autothermal Reforming and Hydrogen Production

Bruno L. D. Santos, W. A. A. Macedo, Camilla D. M. Nickel, Jéssica Florinda Zeitoune, Rafael C. Catapan, Diego Andreazzi Duarte
article en
5 citations

Abstract

This study investigates the development and characterization of Ni-based catalytic monoliths for ethanol reforming, focusing on the effects of incorporating Cu and Pt as promoters. Al2O3 monoliths were coated with α-Al2O3 and impregnated with Ni, Cu, and Pt by using a wet impregnation method. The catalysts were characterized by field-emission scanning electron microscopy (FESEM), energy-dispersive spectroscopy (EDS), X-ray diffraction (XRD), X-ray photoelectron spectroscopy (XPS), and temperature-programmed reduction (TPR). The multitechnique characterization results revealed differences between the monometallic Ni/α-Al2O3 catalyst and the trimetallic Ni-Cu-Pt/α-Al2O3 catalyst. A unique flower-like structure was identified in the trimetallic catalyst, formed due to acid leaching during the Pt impregnation step. The metal impregnation process did not alter the crystalline structure of the Al2O3 substrate with both catalysts primarily exhibiting oxide phases. The Ni-Cu-Pt/α-Al2O3 catalyst has surface concentrations of Cu and Pt around 1.3% or lower, while Ni concentration exceeds 4.8%, confirming the presence of all three metals at the catalyst surface, despite the acid leaching caused by the Pt impregnation. TPR analysis indicated complex metal-support interactions in the trimetallic catalyst, with distinct reduction peaks compared with the monometallic Ni/α-Al2O3 catalyst. Catalytic evaluation revealed that the trimetallic catalyst achieved similar ethanol conversion in comparison with the monometallic Ni/α-Al2O3 catalyst but exhibited lower hydrogen selectivity due to reduced C–C bond breaking, likely influenced by the presence of Cu. These findings highlight the potential and challenges of using trimetallic catalysts in ethanol reforming, with implications for optimizing catalyst composition and reaction conditions for hydrogen production.

Energy & FuelsVol. 38(22)
Universidade Tecnológica Federal do Paraná (BR), Universidade do Estado de Santa Catarina (BR), Universidade Federal de Santa Catarina (BR), Centro de Desenvolvimento da Tecnologia Nuclear (BR)
Conselho Nacional de Desenvolvimento Científico e Tecnológico, Fundação de Amparo à Pesquisa do Estado de Minas Gerais, Fundação de Desenvolvimento da Pesquisa
Openalex Percentile: Top 42%
Catalysts for Methane Reforming
0.53
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