Catalytic Decomposition of Methane to Hydrogen over Al2O3 Supported Mono- and Bimetallic Catalysts

G. E. Ergazieva, N. Makayeva, Z. Shaimerden, S. Soloviev, Мoldir Telbayeva, Еrzhan Akkazin, Fariza Ahmetova
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引用次数: 3

Abstract

This article discusses the decomposition of methane in the temperature range 550–800 °C on low-percentage   monometallic (Ni/g-Al2O3, Co/g-Al2O3) and bimetallic (Ni-Co/g-Al2O3) catalysts. It is shown that the bimetallic catalyst is more active in the decomposition of methane to hydrogen than monometallic ones. At a reaction temperature of 600 °C, the highest methane conversion is 81%, and the highest hydrogen yield of 51% is formed on Ni-Co/g-Al2O3. A complex of physicochemical methods (Scanning Electron Microscope (SEM), X-ray Diffraction (XRD), Temperature Programmed Reduction (TPR-H2), etc.) established that the addition of cobalt oxide to the composition of Ni/g-Al2O3 leads to the formation of surface bimetallic Ni-Co alloys, while the dispersion of particles increases and the reducibility of the catalyst is facilitated, which provides an increase in the concentration of metal particles - active centers, which can be the reason for an increase in the catalytic properties of a bimetallic catalyst in comparison with monometallic ones. Copyright © 2021 by Authors, Published by BCREC Group. This is an open access article under the CC BY-SA License  (https://creativecommons.org/licenses/by-sa/4.0).
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Al2O3负载的单金属和双金属催化剂催化甲烷分解制氢
本文讨论了甲烷在550–800°C的温度范围内在低百分比单金属(Ni/g-Al2O3,Co/g-Al2O3)和双金属(Ni-Co/g-Al2O3)催化剂上的分解。结果表明,双金属催化剂在甲烷分解为氢气方面比单金属催化剂更具活性。在600°C的反应温度下,在Ni-Co/g-Al2O3上形成的甲烷转化率最高为81%,氢气产率最高为51%。复杂的物理化学方法(扫描电子显微镜(SEM)、X射线衍射(XRD)、程序升温还原(TPR-H2)等)证实,在Ni/g-Al2O3的组成中添加氧化钴会导致表面双金属Ni-Co合金的形成,同时颗粒的分散增加,促进了催化剂的还原性,这提供了金属颗粒-活性中心的浓度的增加,这可能是双金属催化剂与单金属催化剂相比催化性能增加的原因。版权所有©2021作者所有,BCREC集团出版。这是CC BY-SA许可证下的开放访问文章(https://creativecommons.org/licenses/by-sa/4.0)。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
CiteScore
3.20
自引率
6.70%
发文量
52
审稿时长
12 weeks
期刊介绍: Bulletin of Chemical Reaction Engineering & Catalysis, a reputable international journal, provides a forum for publishing the novel technologies related to the catalyst, catalysis, chemical reactor, kinetics, and chemical reaction engineering. Scientific articles dealing with the following topics in chemical reaction engineering, catalysis science and engineering, catalyst preparation method and characterization, novel innovation of chemical reactor, kinetic studies, etc. are particularly welcome. However, articles concerned on general chemical engineering process are not covered and out of scope of this journal
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