Coproduction of Hydrogen and Steelmaking Feedstock via Catalytic Methane Pyrolysis over Apricot Shell Char-Supported Iron Catalysts

This study delves into the technical strategy of coproducing hydrogen and steelmaking feedstock through catalytic methane pyrolysis, with the aim of converting the the carbon byproduct from a disposal challenge into a value-added resource. A bifunctional catalyst, namely, apricot shell char-supported iron (ASC/Fe), is devised to combine catalytic function with the product value, allowing the spent catalyst−carbon mixture to be directly utilized as a ferrocarbon feedstock for the steel industry. The structure−activity relationship and catalytic performance are comprehensively investigated. The results indicate that the catalyst attains a high specific surface area of 211.6 m 2 /g subsequent to iron loading, offering abundant active sites and favorable mass transfer channels. At 900 °C and a CH 4 flow rate of 10 mL/min, the ASC/Fe-40 catalyst demonstrates excellent stability over an 11 h period, sustaining a methane conversion above 86%, with a cumulative hydrogen yield of 12,042.1 mL and a carbon yield of 3.11 g. Mechanistic analysis unveils a two-tier “carbon buffering” deactivation mechanism. Initially, metallic iron absorbs active carbon atoms through bulk carburization, thereby delaying surface graphitic encapsulation. Subsequently, iron carbide (C 0.12 Fe 1.88 ) forms as an active intermediate phase that maintains catalytic activity, leading to a gradual rather than an abrupt deactivation. The spent solid product (ASC/Fe@C) is characterized as a composite comprising apricot shell char, metallic iron, iron carbide, and graphitic carbon. Its gasification reactivity in CO 2 is evaluated with respect to its potential as a steelmaking feedstock. Notably, the ASC/Fe@C demonstrates a gasification onset temperature of approximately 850 °C, which is 150 °C lower than that of commercial metallurgical coke. At 900 °C, it achieves a conversion rate of 70.7%, in contrast to only 6.5% for coke. This superior performance is attributed to the intrinsic high reactivity of the apricot shell char matrix and the catalytic activation of CO 2 molecules by the dispersed iron/iron carbide species. In general, this study verifies the feasibility of the “coproduction” concept, providing a new material foundation and technical pathway for coupling clean hydrogen production with low-carbon steelmaking.

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Journal
ACS Sustainable Chemistry & Engineering
Published
2026-06-16
DOI
https://doi.org/10.1021/acssuschemeng.6c03691
Primary Topic
Catalysts for Methane Reforming
Type
article
Field-Weighted Citation Impact
0.00

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article

Coproduction of Hydrogen and Steelmaking Feedstock via Catalytic Methane Pyrolysis over Apricot Shell Char-Supported Iron Catalysts

Zichuan Ma, Hongfang Hao, Dandan Zhao, Xiaolong Ma et al.
ACS Sustainable Chemistry & Engineering
Catalysts for Methane Reforming
article

Coproduction of Hydrogen and Steelmaking Feedstock via Catalytic Methane Pyrolysis over Apricot Shell Char-Supported Iron Catalysts

Zichuan Ma, Hongfang Hao, Dandan Zhao, Xiaolong Ma, Guangyi Lu, Qi Tian
article en

Abstract

This study delves into the technical strategy of coproducing hydrogen and steelmaking feedstock through catalytic methane pyrolysis, with the aim of converting the the carbon byproduct from a disposal challenge into a value-added resource. A bifunctional catalyst, namely, apricot shell char-supported iron (ASC/Fe), is devised to combine catalytic function with the product value, allowing the spent catalyst−carbon mixture to be directly utilized as a ferrocarbon feedstock for the steel industry. The structure−activity relationship and catalytic performance are comprehensively investigated. The results indicate that the catalyst attains a high specific surface area of 211.6 m 2 /g subsequent to iron loading, offering abundant active sites and favorable mass transfer channels. At 900 °C and a CH 4 flow rate of 10 mL/min, the ASC/Fe-40 catalyst demonstrates excellent stability over an 11 h period, sustaining a methane conversion above 86%, with a cumulative hydrogen yield of 12,042.1 mL and a carbon yield of 3.11 g. Mechanistic analysis unveils a two-tier “carbon buffering” deactivation mechanism. Initially, metallic iron absorbs active carbon atoms through bulk carburization, thereby delaying surface graphitic encapsulation. Subsequently, iron carbide (C 0.12 Fe 1.88 ) forms as an active intermediate phase that maintains catalytic activity, leading to a gradual rather than an abrupt deactivation. The spent solid product (ASC/Fe@C) is characterized as a composite comprising apricot shell char, metallic iron, iron carbide, and graphitic carbon. Its gasification reactivity in CO 2 is evaluated with respect to its potential as a steelmaking feedstock. Notably, the ASC/Fe@C demonstrates a gasification onset temperature of approximately 850 °C, which is 150 °C lower than that of commercial metallurgical coke. At 900 °C, it achieves a conversion rate of 70.7%, in contrast to only 6.5% for coke. This superior performance is attributed to the intrinsic high reactivity of the apricot shell char matrix and the catalytic activation of CO 2 molecules by the dispersed iron/iron carbide species. In general, this study verifies the feasibility of the “coproduction” concept, providing a new material foundation and technical pathway for coupling clean hydrogen production with low-carbon steelmaking.

ACS Sustainable Chemistry & Engineering
Shijiazhuang University (CN), Hebei University of Science and Technology (CN), Czech Academy of Sciences, Institute of Inorganic Chemistry (CZ), Hebei Normal University (CN)
National Natural Science Foundation of China, Hebei Normal University
Openalex Percentile: Top 19%
Catalysts for Methane Reforming
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