Cobalt–Nickel Catalysts Supported on Opoka and Diatomite for CO2 Hydrogenation

5 wt % Co–5 wt % Ni catalysts supported on natural opoka and diatomite silica minerals from the Republic of Kazakhstan were prepared via low-temperature combustion and characterized using XRD, SEM/EDS, and BET analyses. The supports primarily comprised various SiO2 modifications, with opoka also containing sodium, magnesium, and iron silicate and aluminosilicate impurities. Diatomite-supported catalysts exhibited specific surface areas ranging from 60.0 to 71.5 m2/g, while for opoka-supported catalysts, it ranged from 28.6 to 62.8 m2/g. During CO2 hydrogenation to methane, the highest conversion (50.9% at 450°C) was achieved with a catalyst supported on untreated diatomite. However, the highest methane selectivity (90.1% at 450°C) was observed for a catalyst supported on opoka calcined at 500°C.

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Publication Details

Journal
International Journal of Self-Propagating High-Temperature Synthesis
Published
2025-11-27
DOI
https://doi.org/10.3103/s1061386225700268
Primary Topic
Catalysts for Methane Reforming
Type
article
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article

Cobalt–Nickel Catalysts Supported on Opoka and Diatomite for CO2 Hydrogenation

E. V. Pugacheva, В. Н. Борщ, I. M. Bystrova, О. D. Boyarchenko et al.
International Journal of Self-Propagating High-Temperature Synthesis
Catalysts for Methane Reforming
article

Cobalt–Nickel Catalysts Supported on Opoka and Diatomite for CO2 Hydrogenation

E. V. Pugacheva, В. Н. Борщ, I. M. Bystrova, О. D. Boyarchenko, N. Yu. Khomenko, S. I. Pomogailo, Rosa I. Jussupkaliyeva
article en

Abstract

5 wt % Co–5 wt % Ni catalysts supported on natural opoka and diatomite silica minerals from the Republic of Kazakhstan were prepared via low-temperature combustion and characterized using XRD, SEM/EDS, and BET analyses. The supports primarily comprised various SiO2 modifications, with opoka also containing sodium, magnesium, and iron silicate and aluminosilicate impurities. Diatomite-supported catalysts exhibited specific surface areas ranging from 60.0 to 71.5 m2/g, while for opoka-supported catalysts, it ranged from 28.6 to 62.8 m2/g. During CO2 hydrogenation to methane, the highest conversion (50.9% at 450°C) was achieved with a catalyst supported on untreated diatomite. However, the highest methane selectivity (90.1% at 450°C) was observed for a catalyst supported on opoka calcined at 500°C.

International Journal of Self-Propagating High-Temperature SynthesisVol. 34(4)
Russian Academy of Sciences (RU), All Russian Institute for Scientific and Technical Information (RU), Zhangir Khan West Kazakhstan Agrarian Technical University (KZ), Institute of Structural Macrokinetics and Materials Science (RU)
Openalex Percentile: Top 75%
Catalysts for Methane Reforming
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Cobalt–Nickel Catalysts Supported on Opoka and Diatomite for CO2 Hydrogenation — E. V. Pugacheva, В. Н. Борщ, et al. · International Journal of Self-Propagating High-Temperature Synthesis (2025) | TGRS Research Map | TGRS