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

Author:

Ergazieva Gaukhar E.12ORCID,Makayeva Nursaya2,Shaimerden Zhanna2,Soloviev Sergiy O.3ORCID,Telbayeva Мoldir1ORCID,Akkazin Еrzhan2,Ahmetova Fariza2

Affiliation:

1. Institute of Combustion Problems, Bogenbay batyra, 172 A, 050012 Almaty , Kazakhstan

2. Al-Farabi Kazakh National University, Al- Farabi ave. 71, 050040 Almaty, Kazakhstan

3. L.V. Pysarzhevskii Institute of Physical Chemistry, National Academy of Sciences of Ukraine, Prospekt Nauki, 31, 03028, Ukraine

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). 

Funder

Science Committee of the Ministry of Education and Science of the Republic of Kazakhstan

Publisher

Bulletin of Chemical Reaction Engineering and Catalysis

Subject

Process Chemistry and Technology,Catalysis

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