Study on iron based Fischer–Tropsch synthesis catalyst supported on mesoporous silica promoted by alkali and transition metals

Fischer Tropsch synthesis provides a non-petroleum pathway for the production of high value liquid fuels and long-chain alpha olefins from syngas. However, regulating product distribution to promote the formation of high value product while maintaining low selectivity for C1 by-products (CH4 and CO2) remains a significant challenge. Iron based composite catalysts were prepared via dual doping and modification, i.e., alkali metals and transition metals using mesoporous silica SBA-15 as the support. The catalyst was characterized by XPS, XRD, H2-TPR, CO2-TPD, TEM, Roman and other methods, and the relationship between the catalyst structure and catalytic performance was studied. At 1 MPa and 300 °C, The CO conversion rate of Fe–Zn–K/SBA-15 (30% − 10% 2%/100%) catalyst is 62.4%, methane selectivity is reduced to 4.6%, carbon dioxide selectivity is 32.6%, olefin ratio is 7.6%, and long-chain hydrocarbon C5 + selectivity is 62.8%.

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Publication Details

Journal
Discover Chemical Engineering
Published
2025-04-23
DOI
https://doi.org/10.1007/s43938-025-00081-0
Citations
2
Primary Topic
Catalysts for Methane Reforming
Type
article
Field-Weighted Citation Impact
0.78

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article

Study on iron based Fischer–Tropsch synthesis catalyst supported on mesoporous silica promoted by alkali and transition metals

Pengfei Feng, Mingqiang Chen, Luya Zhang, Quan Wang et al.
2 citations
Discover Chemical Engineering
Catalysts for Methane Reforming
0.78
article

Study on iron based Fischer–Tropsch synthesis catalyst supported on mesoporous silica promoted by alkali and transition metals

Pengfei Feng, Mingqiang Chen, Luya Zhang, Quan Wang, Jun Wang, Peng Wang, Yishuang Wang, Zewan Bao, Xuemei Shen
article en
2 citations

Abstract

Fischer Tropsch synthesis provides a non-petroleum pathway for the production of high value liquid fuels and long-chain alpha olefins from syngas. However, regulating product distribution to promote the formation of high value product while maintaining low selectivity for C1 by-products (CH4 and CO2) remains a significant challenge. Iron based composite catalysts were prepared via dual doping and modification, i.e., alkali metals and transition metals using mesoporous silica SBA-15 as the support. The catalyst was characterized by XPS, XRD, H2-TPR, CO2-TPD, TEM, Roman and other methods, and the relationship between the catalyst structure and catalytic performance was studied. At 1 MPa and 300 °C, The CO conversion rate of Fe–Zn–K/SBA-15 (30% − 10% 2%/100%) catalyst is 62.4%, methane selectivity is reduced to 4.6%, carbon dioxide selectivity is 32.6%, olefin ratio is 7.6%, and long-chain hydrocarbon C5 + selectivity is 62.8%.

Discover Chemical EngineeringVol. 5(1)
Anhui University of Science and Technology (CN), Coal Industry Jinan Design & Research Institute (China) (CN), National Institute of Clean and Low-Carbon Energy (CN)
National Key Research and Development Program of China
Openalex Percentile: Top 32%
Catalysts for Methane Reforming
0.78
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