LAPSE:2024.1695v1
Published Article

LAPSE:2024.1695v1
Effect of Support on Steam Reforming of Ethanol for H2 Production with Copper-Based Catalysts
August 23, 2024
Abstract
Catalytic studies hydrogen production via steam reforming of ethanol (SRE) are essential for process optimization. Likewise, selecting the ideal support for the active phase can be critical to achieve high conversion rates during the catalytic steam reforming process. In this work, copper-based catalysts were synthesized using two different supports, NaY zeolite and Nb2O5/Al2O3 mixed oxides. The materials were prepared using wet impregnation and characterized for their physicochemical properties using different analytical techniques. Differences in the catalyst morphologies were readily attributed to the characteristics of the support. The Cu/NaY catalyst exhibited a higher specific surface area (210.40 m2 g−1) compared to the Cu/Nb2O5/Al2O3 catalyst (26.00 m2 g−1), resulting in a homogeneous metal dispersion over the support surface. The obtained results showed that, at 300 °C, both the Cu/Nb2O5/Al2O3 and Cu/NaY catalysts produced approximately 50% hydrogen and 40% acetaldehyde, but with significant differences in conversion (6% and 56%, respectively). At 450 °C, a greater product distribution and a 10% higher conversion were observed when the catalyst was supported on NaY compared to Nb2O5/Al2O3. Hence, the performance of copper-based catalysts was influenced significantly by the textural properties of the support.
Catalytic studies hydrogen production via steam reforming of ethanol (SRE) are essential for process optimization. Likewise, selecting the ideal support for the active phase can be critical to achieve high conversion rates during the catalytic steam reforming process. In this work, copper-based catalysts were synthesized using two different supports, NaY zeolite and Nb2O5/Al2O3 mixed oxides. The materials were prepared using wet impregnation and characterized for their physicochemical properties using different analytical techniques. Differences in the catalyst morphologies were readily attributed to the characteristics of the support. The Cu/NaY catalyst exhibited a higher specific surface area (210.40 m2 g−1) compared to the Cu/Nb2O5/Al2O3 catalyst (26.00 m2 g−1), resulting in a homogeneous metal dispersion over the support surface. The obtained results showed that, at 300 °C, both the Cu/Nb2O5/Al2O3 and Cu/NaY catalysts produced approximately 50% hydrogen and 40% acetaldehyde, but with significant differences in conversion (6% and 56%, respectively). At 450 °C, a greater product distribution and a 10% higher conversion were observed when the catalyst was supported on NaY compared to Nb2O5/Al2O3. Hence, the performance of copper-based catalysts was influenced significantly by the textural properties of the support.
Record ID
Keywords
copper-based catalysts, ethanol steam reforming, hydrogen production, mixed oxides, zeolite
Subject
Suggested Citation
Nippes RP, Macruz PD, Domingues Gomes A, de Souza M, Ferreira BR, Rizzo-Domingues RCP, Pereira Ramos L. Effect of Support on Steam Reforming of Ethanol for H2 Production with Copper-Based Catalysts. (2024). LAPSE:2024.1695v1
Author Affiliations
Nippes RP: Graduate Program in Chemical Engineering, Federal University of Parana, R. Francisco H. dos Santos, Curitiba 81531-990, Paraná, Brazil [ORCID]
Macruz PD: Department of Chemical Engineering, Maringa State University, Av. Colombo, 5790, Maringá 87020-900, Paraná, Brazil
Domingues Gomes A: Department of Chemical Engineering, Maringa State University, Av. Colombo, 5790, Maringá 87020-900, Paraná, Brazil [ORCID]
de Souza M: Department of Chemical Engineering, Maringa State University, Av. Colombo, 5790, Maringá 87020-900, Paraná, Brazil
Ferreira BR: Department of Chemical and Biology, Federal Technology University of Paraná, Av. Heitor de Alencar Furtado, 5000, Curitiba 81280-340, Paraná, Brazil
Rizzo-Domingues RCP: Department of Chemical and Biology, Federal Technology University of Paraná, Av. Heitor de Alencar Furtado, 5000, Curitiba 81280-340, Paraná, Brazil [ORCID]
Pereira Ramos L: Graduate Program in Chemical Engineering, Federal University of Parana, R. Francisco H. dos Santos, Curitiba 81531-990, Paraná, Brazil [ORCID]
Macruz PD: Department of Chemical Engineering, Maringa State University, Av. Colombo, 5790, Maringá 87020-900, Paraná, Brazil
Domingues Gomes A: Department of Chemical Engineering, Maringa State University, Av. Colombo, 5790, Maringá 87020-900, Paraná, Brazil [ORCID]
de Souza M: Department of Chemical Engineering, Maringa State University, Av. Colombo, 5790, Maringá 87020-900, Paraná, Brazil
Ferreira BR: Department of Chemical and Biology, Federal Technology University of Paraná, Av. Heitor de Alencar Furtado, 5000, Curitiba 81280-340, Paraná, Brazil
Rizzo-Domingues RCP: Department of Chemical and Biology, Federal Technology University of Paraná, Av. Heitor de Alencar Furtado, 5000, Curitiba 81280-340, Paraná, Brazil [ORCID]
Pereira Ramos L: Graduate Program in Chemical Engineering, Federal University of Parana, R. Francisco H. dos Santos, Curitiba 81531-990, Paraná, Brazil [ORCID]
Journal Name
Processes
Volume
12
Issue
7
First Page
1331
Year
2024
Publication Date
2024-06-27
ISSN
2227-9717
Version Comments
Original Submission
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PII: pr12071331, Publication Type: Journal Article
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LAPSE:2024.1695v1
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https://doi.org/10.3390/pr12071331
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Aug 23, 2024
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Aug 23, 2024
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