Insight of oil-soluble Fe-based catalyst for direct liquefaction of Shangwan coal

IF 7.5 1区 工程技术 Q2 ENERGY & FUELS Fuel Pub Date : 2025-03-15 Epub Date: 2024-12-02 DOI:10.1016/j.fuel.2024.133951
Zhi Li , Yuxin Wen , Rui Zhang , Mei Zhong , Haiyun Liu , Xin Zheng , Haoquan Hu , Lijun Jin
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Abstract

Oil-soluble Fe-based catalysts with different carbon numbers of ligand were prepared to investigate the action mechanism of oil-soluble catalyst on direct coal liquefaction. Results showed that the increment of ligand carbon numbers decreased the average grain size of active phase Fe1-xS, promoted activation of gaseous and solvent hydrogen and coal conversion into oil. Oil yield was remarkably increased from 57 wt% to 68 wt% with increasing carbon number in ligand from 8 to 18. A linear relationship between oil yield and oil-wetness of Fe-based catalysts was constructed. Ligand and Fe contributed to oil yield increment about by 5 wt% and 10 wt%, respectively. Oil yield was enhanced via participating in annihilation of coal pyrolysis free radicals by H-rich radicals from cleavage of oil-soluble ligands. When highly active iron stearate was used, almost similar oil yield at initial H2 pressure of 6.50 MPa as that under 7.00 MPa indicated that liquefaction condition could be alleviated.
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上湾煤直接液化油溶性铁基催化剂的研究进展
制备了不同配体碳数的油溶性铁基催化剂,研究了油溶性催化剂对煤直接液化的作用机理。结果表明,配体碳数的增加降低了Fe1-xS的平均晶粒尺寸,促进了气态氢和溶剂氢的活化和煤转化为油。随着配体碳数从8个增加到18个,油收率从57 wt%显著提高到68 wt%。建立了铁基催化剂的产油率与油湿性之间的线性关系。配体和铁对油收率的贡献分别为5 wt%和10 wt%。油溶性配体裂解产生的富h自由基参与煤热解自由基的湮灭,从而提高了油收率。当使用高活性硬脂酸铁时,在初始H2压力为6.50 MPa时的产油率与在初始H2压力为7.00 MPa时的产油率基本一致,表明液化条件可以得到缓解。
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来源期刊
Fuel
Fuel 工程技术-工程:化工
CiteScore
12.80
自引率
20.30%
发文量
3506
审稿时长
64 days
期刊介绍: The exploration of energy sources remains a critical matter of study. For the past nine decades, fuel has consistently held the forefront in primary research efforts within the field of energy science. This area of investigation encompasses a wide range of subjects, with a particular emphasis on emerging concerns like environmental factors and pollution.
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