Regulating Iron Carbide Evolution over CNT-Supported Fe Catalysts by Mn Incorporation for Selective CO Hydrogenation to Linear α-Olefins

Linear α-olefins (LAOs) from CO/H2 represent an attractive non-petroleum route, yet their selective formation over Fe catalysts is often limited by CO2 formation via water–gas shift (WGS) reaction and by secondary hydrogenation that consumes terminal olefins. In this work, we demonstrate that these competing pathways can be regulated on carbon-nanotube (CNT) supported Fe catalysts by controlling the CNT interfacial oxygen environment through NO treatment or high-temperature annealing and by adjusting the Mn incorporation protocol between co-impregnation and stepwise addition. Under identical reaction conditions at 280 °C and 3.0 MPa with an H2-to-CO ratio of 1, high-temperature treated CNTs improve olefin preservation and LAO retention compared with NO-treated CNTs. Mn promotion further shifts selectivity toward α-olefins and lowers CO2 selectivity. At the same Fe-to-Mn ratio, the Mn introduction sequence produces distinct reducibility and CO-binding behaviors that lead to different steady-state oxide and carbide phases. XPS, H2-TPR, and CO-TPD collectively suggest that CNT pretreatment and the Mn protocol modulate near-surface oxygen speciation, reduction kinetics, and CO adsorption strength. Mössbauer spectroscopy confirms a predominantly χ-Fe5C2 population and indicates the presence of ε-Fe2C in selected samples together with residual oxide and superparamagnetic Fe species. These results highlight the importance of controlling the CNT–metal interface and Mn–Fe proximity to enhance LAO retention under high-temperature CO hydrogenation.

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Publication Details

Journal
Catalysts
Published
2026-03-05
DOI
https://doi.org/10.3390/catal16030244
Primary Topic
Catalysts for Methane Reforming
Type
article
Field-Weighted Citation Impact
0.00

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article

Regulating Iron Carbide Evolution over CNT-Supported Fe Catalysts by Mn Incorporation for Selective CO Hydrogenation to Linear α-Olefins

Yanan Sun, Yi-Xiang Wang, Zixing Shi, Qiwen Sun et al.
Catalysts
Catalysts for Methane Reforming
article

Regulating Iron Carbide Evolution over CNT-Supported Fe Catalysts by Mn Incorporation for Selective CO Hydrogenation to Linear α-Olefins

Yanan Sun, Yi-Xiang Wang, Zixing Shi, Qiwen Sun, Hengxuan Zhang
article en

Abstract

Linear α-olefins (LAOs) from CO/H2 represent an attractive non-petroleum route, yet their selective formation over Fe catalysts is often limited by CO2 formation via water–gas shift (WGS) reaction and by secondary hydrogenation that consumes terminal olefins. In this work, we demonstrate that these competing pathways can be regulated on carbon-nanotube (CNT) supported Fe catalysts by controlling the CNT interfacial oxygen environment through NO treatment or high-temperature annealing and by adjusting the Mn incorporation protocol between co-impregnation and stepwise addition. Under identical reaction conditions at 280 °C and 3.0 MPa with an H2-to-CO ratio of 1, high-temperature treated CNTs improve olefin preservation and LAO retention compared with NO-treated CNTs. Mn promotion further shifts selectivity toward α-olefins and lowers CO2 selectivity. At the same Fe-to-Mn ratio, the Mn introduction sequence produces distinct reducibility and CO-binding behaviors that lead to different steady-state oxide and carbide phases. XPS, H2-TPR, and CO-TPD collectively suggest that CNT pretreatment and the Mn protocol modulate near-surface oxygen speciation, reduction kinetics, and CO adsorption strength. Mössbauer spectroscopy confirms a predominantly χ-Fe5C2 population and indicates the presence of ε-Fe2C in selected samples together with residual oxide and superparamagnetic Fe species. These results highlight the importance of controlling the CNT–metal interface and Mn–Fe proximity to enhance LAO retention under high-temperature CO hydrogenation.

CatalystsVol. 16(3)
China Coal Technology and Engineering Group Corp (China) (CN), Taiyuan University of Technology (CN)
National Key Research and Development Program of China
Openalex Percentile: Top 34%
Catalysts for Methane Reforming
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