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Xicai Liu, Jue Tang, Mansheng Chu, Zichuan Zhao, Jinge Feng, and Jie Liu, Mechanistic insights into H2 and CO interactions with Fe3O4(111) surface: A computational study for hydrogen-based direct reduction process, Int. J. Miner. Metall. Mater., (2025). https://doi.org/10.1007/s12613-025-3183-x
Xicai Liu, Jue Tang, Mansheng Chu, Zichuan Zhao, Jinge Feng, and Jie Liu, Mechanistic insights into H2 and CO interactions with Fe3O4(111) surface: A computational study for hydrogen-based direct reduction process, Int. J. Miner. Metall. Mater., (2025). https://doi.org/10.1007/s12613-025-3183-x
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H2和CO与Fe3O4(111)表面相互作用的机理:氢基直接还原过程的计算研究

摘要: 氢基竖炉工艺因其可以显著减少CO2排放备受关注。本研究基于密度泛函理论方法,对氢基竖炉条件下H2和CO与Fetet1-和Feoct2-端Fe3O4(111)表面的相互作用机制进行系统研究,包括其吸附和还原行为。结果表明,H2分子在Fetet1-端表面的吸附能为−1.36 eV,而CO分子则更倾向于在Feoct2-端表面上吸附,其吸附能为−1.56 eV。H2和CO均在Fetet1-端表面更易发生还原反应(能垒分别为0.83 eV 和2.23 eV),并且从动力学角度来看,H2的反应比CO更有利。在400至1400 K的热力学条件下,H2易在Fetet1-端表面吸附,而CO则倾向于在此表面上发生反应。在Feoct2-端表面上,这些热力学趋势则相反。H2在Fetet1-端表面反应的热力学劣势可通过提高温度来弥补。此外,共吸附计算结果表明,H2和CO在Fetet1-端表面上的吸附是竞争的,而在Feoct2-端表面上的吸附则是协同的。综上表明,具有较高比例的Fetet1-端表面的铁矿石可用于氢基竖炉工艺,同时,升高还原温度并提高还原气体H2比例可以促进氢基竖炉的高效冶炼。以上结果为优化实际操作参数和推进氢基竖炉工艺的发展提供了有效指导。

 

Mechanistic insights into H2 and CO interactions with Fe3O4(111) surface: A computational study for hydrogen-based direct reduction process

Abstract: The novel process of hydrogen-based shaft furnaces (HSFs) has attracted considerable attention because of their significant reduction of CO2 emissions. In this study, the interaction of H2 and CO with Fetet1- and Feoct2-terminated Fe3O4(111) surfaces under HSF conditions, including their adsorption and reduction behaviors, was investigated using the density functional theory method. The results indicated that the H2 molecule adsorbed onto the Fetet1-terminated surface with an adsorption energy (AE) of −1.36 eV, whereas the CO molecule preferentially adsorbed on the Feoct2-terminated surface with an AE of −1.56 eV. Both H2 and CO can readily undergo reduction on the Fetet1-terminated surface (corresponding to energy barriers of 0.83 eV and 2.23 eV, respectively), but kinetically the reaction of H2 is more favorable than that of CO. With regard to the thermodynamics at 400–1400 K, the H2 was easy to be adsorbed, while the CO would like to react on the Fetet1-terminated surface. These thermodynamically tendencies were reversed on the Feoct2-terminated surface. The thermodynamic disadvantage of the reaction of H2 on the Fetet1-terminated surface was offset by an increase in the temperature. Furthermore, the adsorption of H2 and CO on the Fetet1-terminated surface was competitive, whereas the adsorption of them on the Feoct2-terminated surface was synergistic. Therefore, iron ores with a higher proportion of Fetet1-terminated surface can be applied for the HSF process. In conjunction with the increase in reduction temperature, the increase in the ratio of H2 in the reducing gas would promote efficient HSF smelting. These observations provide effective guidance for optimizing the practical operation parameters and advancing the development of the HSF process.

 

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