1. National Engineering Research Center for Direct Coal Liquefaction,Shanghai,201108
2. CHN Energy Cornerstone Chemical Technology (Shanghai) Co., Ltd
纸质出版:2025
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Dao Li, Shansong Gao, Xu Li, 等. Syntheses and characterizations of oil-soluble iron-based catalysts for direct coal liquefaction[J]. 清洁能源(英文), 2025,(5).
Dao Li, Shansong Gao, Xu Li, Chunlan Xiang, Xiaojun Duan, Jing Xie, Xiangfeng Yu, Syntheses and characterizations of oil-soluble iron-based catalysts for direct coal liquefaction, Clean Energy, Volume 9, Issue 5, October 2025, Pages 136–148, https://doi.org/10.1093/ce/zkaf041
Dao Li, Shansong Gao, Xu Li, 等. Syntheses and characterizations of oil-soluble iron-based catalysts for direct coal liquefaction[J]. 清洁能源(英文), 2025,(5). DOI: 10.1093/ce/zkaf041.
Dao Li, Shansong Gao, Xu Li, Chunlan Xiang, Xiaojun Duan, Jing Xie, Xiangfeng Yu, Syntheses and characterizations of oil-soluble iron-based catalysts for direct coal liquefaction, Clean Energy, Volume 9, Issue 5, October 2025, Pages 136–148, https://doi.org/10.1093/ce/zkaf041 DOI:
Iron-based catalysts have been one of the most active fields in coal direct liquefaction technology due to their advantages of a vast source of raw materials
low synthesis cost
and high catalytic activities. In this study
five oil-soluble iron-based catalysts with different carbon chain lengths were synthesized by reacting a series of fatty acid sodium salts with trivalent iron salts as raw materials. The catalyst precursors synthesized were structurally characterized using inductively coupled plasma emission spectroscopy
Fourier transform infrared spectroscopy
and high-resolution mass spectrometry. In the presulfurization and activity evaluation experiments of coal direct liquefaction carried out in an autoclave
it was found by X-ray diffraction transmission electron microscopy and X-ray photoelectron spectrometry that the iron oleate catalysts formed highly catalytic Fe1−xS phases during the sulfurization process
with average particle sizes of ∼200–300 nm and uniform distribution. The results of catalyst activity evaluation showed that under the same reaction conditions (temperature 455°C
reaction pressure 19 MPa
residence time 60 min) and
with the same addition amount of m(Fe)/m(dry coal) = 1%
the iron oleate catalyst exhibited excellent catalytic performance
with a coal conversion of 89.45% and an extraction oil yield of 64.04%
which was significantly better than that of other oil-soluble iron-based catalysts. It is worth noting that the iron oleate catalyst can achieve comparable catalytic performance at a lower addition amount (m(Fe)/m(dry coal) = 0.5 wt%) compared with the ultrafine hydrated iron oxide (FeOOH) catalyst
which requires an addition amount of m(Fe)/m(dry coal) = 1 wt%. This not only reduces the cost of catalyst usage but also simplifies the subsequent dehydration and drying processes. The findings of this study hold significant importance for the development of new
high-efficiency catalysts for coal direct liquefaction and offer a theoretical foundation and technical support for the industrial application of coal-to-liquid technology.
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