Effect of Shell Thickness on the Catalytic Performance of Co@SiO<sub>2</sub> Core‐Shell Catalysts for Fischer–Tropsch Synthesis

ABSTRACT Fischer–Tropsch synthesis (FTS) is an essential strategy for mitigating the energy crisis, combating climate change, and promoting sustainable development. Supported cobalt‐based catalysts exhibit significant activity in FTS, but their product selectivity requires further optimization. In this paper, Co@SiO 2 catalysts with core‐shell structure were prepared by hydrothermal synthesis. The effect of the SiO 2 shell thickness on the catalytic performance of FTS was explored by varying the amount of ethyl orthosilicate (TEOS) added with stabilizer polyvinylpyrrolidone (PVP). Among them, the catalyst CS3 achieved the greatest number of cobalt active sites, the highest CO conversion (77.2%), and C 5+ selectivity (84.3%) with a high C 5 ‐C 11 proportion in the C 5+ product. Characterizations of the catalysts were performed to examine their morphology and physicochemical properties. It was observed that the dispersion of cobalt species improved with increasing shell thickness within a certain range, promoting the reduction of cobalt species. However, the formation of Si‐OH groups because of the hydrolysis of excess TEOS clogged catalyst pores, consequently diminishing the catalytic activity in FTS. Compared with the CS3‐PVP0 catalyst without stabilizer PVP added, the catalyst CS3 with PVP added exhibited obvious ordered morphology, making CO conversion significantly enhanced. This is attributed to the role of inert carbon in PVP, which not only boosts the reducibility of cobalt species but also enhances the surface hydrophobicity of the mesoporous SiO 2 material.

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Publication Details

Journal
Applied Organometallic Chemistry
Published
2025-02-13
DOI
https://doi.org/10.1002/aoc.70068
Citations
2
Primary Topic
Catalysts for Methane Reforming
Type
article
Field-Weighted Citation Impact
0.78

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article

Effect of Shell Thickness on the Catalytic Performance of Co@SiO2 Core‐Shell Catalysts for Fischer–Tropsch Synthesis

Tao Chen, Xin Wang, Zhenhua Li
2 citations
Applied Organometallic Chemistry
Catalysts for Methane Reforming
0.78
article

Effect of Shell Thickness on the Catalytic Performance of Co@SiO2 Core‐Shell Catalysts for Fischer–Tropsch Synthesis

Tao Chen, Xin Wang, Zhenhua Li
article en
2 citations

Abstract

ABSTRACT Fischer–Tropsch synthesis (FTS) is an essential strategy for mitigating the energy crisis, combating climate change, and promoting sustainable development. Supported cobalt‐based catalysts exhibit significant activity in FTS, but their product selectivity requires further optimization. In this paper, Co@SiO 2 catalysts with core‐shell structure were prepared by hydrothermal synthesis. The effect of the SiO 2 shell thickness on the catalytic performance of FTS was explored by varying the amount of ethyl orthosilicate (TEOS) added with stabilizer polyvinylpyrrolidone (PVP). Among them, the catalyst CS3 achieved the greatest number of cobalt active sites, the highest CO conversion (77.2%), and C 5+ selectivity (84.3%) with a high C 5 ‐C 11 proportion in the C 5+ product. Characterizations of the catalysts were performed to examine their morphology and physicochemical properties. It was observed that the dispersion of cobalt species improved with increasing shell thickness within a certain range, promoting the reduction of cobalt species. However, the formation of Si‐OH groups because of the hydrolysis of excess TEOS clogged catalyst pores, consequently diminishing the catalytic activity in FTS. Compared with the CS3‐PVP0 catalyst without stabilizer PVP added, the catalyst CS3 with PVP added exhibited obvious ordered morphology, making CO conversion significantly enhanced. This is attributed to the role of inert carbon in PVP, which not only boosts the reducibility of cobalt species but also enhances the surface hydrophobicity of the mesoporous SiO 2 material.

Applied Organometallic ChemistryVol. 39(3)
Tianjin University (CN)
National Natural Science Foundation of China
Openalex Percentile: Top 34%
Catalysts for Methane Reforming
0.78
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