Zhi Li , Yuxin Wen , Rui Zhang , Mei Zhong , Haiyun Liu , Xin Zheng , Haoquan Hu , Lijun Jin
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引用次数: 0
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.
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.