Catalytic performance of Ni-Cu/Al2O3 for effective syngas production by methanol steam reforming

Martin Khzouz; Evangelos Gkanas; Shangfeng  Du; Joe Wood

doi:10.1016/j.fuel.2018.06.025

Catalytic performance of Ni-Cu/Al2O3 for effective syngas production by methanol steam reforming

Martin Khzouz, Evangelos Gkanas, Shangfeng Du, Joe Wood

Institute for Future Transport and Cities

Research output: Contribution to journal › Article › peer-review

33 Citations (Scopus)

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Abstract

This work investigates the catalytic performance of bimetallic Ni-Cu/Al2O3 catalysts for syngas production by methanol steam reforming. The synthesis and characterization of a series of Nix-Cuy/Al2O3 catalysts with various stoichiometric fractions (x = 10, 7, 5, 3 and 0 wt% and y = 0, 3, 5, 7 and 10 wt% to Al2O3 support, respectively) are investigated and discussed. The catalytic performance is evaluated experimentally at temperature range of 225–325 °C. Both mono-metallic catalyst (10wt%Cu/Al2O3 and 10wt%Ni/Al2O3) and bi-metallic catalysts (7wt%Cu-3wt%Ni/Al2O3, 5wt%Cu-5wt%Ni/Al2O3 and 3wt%Cu-7wt%Ni/Al2O3) are synthesized using an impregnation method and characterized by means of SEM, temperature programmed reduction (TPR), BET analysis, XRD and TGA. It is found that the bimetallic Ni-Cu catalyst had a strong influence on the amount of CO2 and CO produced due to the different selectivity towards the water gas shift reaction and methanol decomposition reaction. The increase of the Ni content leads to an increase in CO and decrease in CO2 yields. The bimetallic catalyst did not produce CH4, revealing that Cu alloying in Ni catalyst had an inhibiting effect for CO and/or CO2 hydrogenation

Original language	English
Pages (from-to)	672–683
Number of pages	11
Journal	Fuel
Volume	232
Early online date	14 Jun 2018
DOIs	https://doi.org/10.1016/j.fuel.2018.06.025
Publication status	Published - 15 Nov 2018

Bibliographical note

NOTICE: this is the author’s version of a work that was accepted for publication in Fuel. Changes resulting from the publishing process, such as peer review, editing, corrections, structural formatting, and other quality control mechanisms may not be reflected in this document. Changes may have been made to this work since it was submitted for publication. A definitive version was subsequently published in Fuel, [232], (2018)] DOI: 10.1016/j.fuel.2018.06.025

© 2018, Elsevier. Licensed under the Creative Commons Attribution-NonCommercial-NoDerivatives 4.0 International http://creativecommons.org/licenses/by-nc-nd/4.0/

Copyright © and Moral Rights are retained by the author(s) and/ or other copyright owners. A copy can be downloaded for personal non-commercial research or study, without prior permission or charge. This item cannot be reproduced or quoted extensively from without first obtaining permission in writing from the copyright holder(s). The content must not be changed in any way or sold commercially in any format or medium without the formal permission of the copyright holders.

Keywords

Steam reformer
Characterisation
Ni-Cu/Al2O3
Methanol reforming catalyst
Methanol steam reforming
Syngas production

Access to Document

10.1016/j.fuel.2018.06.025

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https://research.birmingham.ac.uk/portal/en/publications/catalytic-performance-of-nicual2o3-for-effective-syngas-production-by-methanol-steam-reforming(76d4f211-28f8-42e6-8b17-5aa127fdd9b3).htmlLicence: CC BY-NC-ND

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@article{42f153fe9e8846a48c59075da35ee7f8,

title = "Catalytic performance of Ni-Cu/Al2O3 for effective syngas production by methanol steam reforming",

abstract = "This work investigates the catalytic performance of bimetallic Ni-Cu/Al2O3 catalysts for syngas production by methanol steam reforming. The synthesis and characterization of a series of Nix-Cuy/Al2O3 catalysts with various stoichiometric fractions (x = 10, 7, 5, 3 and 0 wt% and y = 0, 3, 5, 7 and 10 wt% to Al2O3 support, respectively) are investigated and discussed. The catalytic performance is evaluated experimentally at temperature range of 225–325 °C. Both mono-metallic catalyst (10wt%Cu/Al2O3 and 10wt%Ni/Al2O3) and bi-metallic catalysts (7wt%Cu-3wt%Ni/Al2O3, 5wt%Cu-5wt%Ni/Al2O3 and 3wt%Cu-7wt%Ni/Al2O3) are synthesized using an impregnation method and characterized by means of SEM, temperature programmed reduction (TPR), BET analysis, XRD and TGA. It is found that the bimetallic Ni-Cu catalyst had a strong influence on the amount of CO2 and CO produced due to the different selectivity towards the water gas shift reaction and methanol decomposition reaction. The increase of the Ni content leads to an increase in CO and decrease in CO2 yields. The bimetallic catalyst did not produce CH4, revealing that Cu alloying in Ni catalyst had an inhibiting effect for CO and/or CO2 hydrogenation",

keywords = "Steam reformer, Characterisation, Ni-Cu/Al2O3, Methanol reforming catalyst, Methanol steam reforming, Syngas production",

author = "Martin Khzouz and Evangelos Gkanas and Shangfeng Du and Joe Wood",

note = "NOTICE: this is the author{\textquoteright}s version of a work that was accepted for publication in Fuel. Changes resulting from the publishing process, such as peer review, editing, corrections, structural formatting, and other quality control mechanisms may not be reflected in this document. Changes may have been made to this work since it was submitted for publication. A definitive version was subsequently published in Fuel, [232], (2018)] DOI: 10.1016/j.fuel.2018.06.025 {\textcopyright} 2018, Elsevier. Licensed under the Creative Commons Attribution-NonCommercial-NoDerivatives 4.0 International http://creativecommons.org/licenses/by-nc-nd/4.0/ Copyright {\textcopyright} and Moral Rights are retained by the author(s) and/ or other copyright owners. A copy can be downloaded for personal non-commercial research or study, without prior permission or charge. This item cannot be reproduced or quoted extensively from without first obtaining permission in writing from the copyright holder(s). The content must not be changed in any way or sold commercially in any format or medium without the formal permission of the copyright holders. ",

year = "2018",

month = nov,

day = "15",

doi = "10.1016/j.fuel.2018.06.025",

language = "English",

volume = "232",

pages = "672–683",

journal = "Fuel",

issn = "0016-2361",

publisher = "Elsevier",

}

TY - JOUR

T1 - Catalytic performance of Ni-Cu/Al2O3 for effective syngas production by methanol steam reforming

AU - Khzouz, Martin

AU - Gkanas, Evangelos

AU - Du, Shangfeng

AU - Wood, Joe

N1 - NOTICE: this is the author’s version of a work that was accepted for publication in Fuel. Changes resulting from the publishing process, such as peer review, editing, corrections, structural formatting, and other quality control mechanisms may not be reflected in this document. Changes may have been made to this work since it was submitted for publication. A definitive version was subsequently published in Fuel, [232], (2018)] DOI: 10.1016/j.fuel.2018.06.025 © 2018, Elsevier. Licensed under the Creative Commons Attribution-NonCommercial-NoDerivatives 4.0 International http://creativecommons.org/licenses/by-nc-nd/4.0/ Copyright © and Moral Rights are retained by the author(s) and/ or other copyright owners. A copy can be downloaded for personal non-commercial research or study, without prior permission or charge. This item cannot be reproduced or quoted extensively from without first obtaining permission in writing from the copyright holder(s). The content must not be changed in any way or sold commercially in any format or medium without the formal permission of the copyright holders.

PY - 2018/11/15

Y1 - 2018/11/15

N2 - This work investigates the catalytic performance of bimetallic Ni-Cu/Al2O3 catalysts for syngas production by methanol steam reforming. The synthesis and characterization of a series of Nix-Cuy/Al2O3 catalysts with various stoichiometric fractions (x = 10, 7, 5, 3 and 0 wt% and y = 0, 3, 5, 7 and 10 wt% to Al2O3 support, respectively) are investigated and discussed. The catalytic performance is evaluated experimentally at temperature range of 225–325 °C. Both mono-metallic catalyst (10wt%Cu/Al2O3 and 10wt%Ni/Al2O3) and bi-metallic catalysts (7wt%Cu-3wt%Ni/Al2O3, 5wt%Cu-5wt%Ni/Al2O3 and 3wt%Cu-7wt%Ni/Al2O3) are synthesized using an impregnation method and characterized by means of SEM, temperature programmed reduction (TPR), BET analysis, XRD and TGA. It is found that the bimetallic Ni-Cu catalyst had a strong influence on the amount of CO2 and CO produced due to the different selectivity towards the water gas shift reaction and methanol decomposition reaction. The increase of the Ni content leads to an increase in CO and decrease in CO2 yields. The bimetallic catalyst did not produce CH4, revealing that Cu alloying in Ni catalyst had an inhibiting effect for CO and/or CO2 hydrogenation

AB - This work investigates the catalytic performance of bimetallic Ni-Cu/Al2O3 catalysts for syngas production by methanol steam reforming. The synthesis and characterization of a series of Nix-Cuy/Al2O3 catalysts with various stoichiometric fractions (x = 10, 7, 5, 3 and 0 wt% and y = 0, 3, 5, 7 and 10 wt% to Al2O3 support, respectively) are investigated and discussed. The catalytic performance is evaluated experimentally at temperature range of 225–325 °C. Both mono-metallic catalyst (10wt%Cu/Al2O3 and 10wt%Ni/Al2O3) and bi-metallic catalysts (7wt%Cu-3wt%Ni/Al2O3, 5wt%Cu-5wt%Ni/Al2O3 and 3wt%Cu-7wt%Ni/Al2O3) are synthesized using an impregnation method and characterized by means of SEM, temperature programmed reduction (TPR), BET analysis, XRD and TGA. It is found that the bimetallic Ni-Cu catalyst had a strong influence on the amount of CO2 and CO produced due to the different selectivity towards the water gas shift reaction and methanol decomposition reaction. The increase of the Ni content leads to an increase in CO and decrease in CO2 yields. The bimetallic catalyst did not produce CH4, revealing that Cu alloying in Ni catalyst had an inhibiting effect for CO and/or CO2 hydrogenation

KW - Steam reformer

KW - Characterisation

KW - Ni-Cu/Al2O3

KW - Methanol reforming catalyst

KW - Methanol steam reforming

KW - Syngas production

U2 - 10.1016/j.fuel.2018.06.025

DO - 10.1016/j.fuel.2018.06.025

M3 - Article

VL - 232

SP - 672

EP - 683

JO - Fuel

JF - Fuel

SN - 0016-2361

ER -