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Nitrogen-doped carbon supported iron nanoparticles for mild catalytic hydrocracking of Xilinguole lignite
被引:0
|作者:
Yang, Zhi
[1
]
Liu, Fang-Jing
[1
,2
,3
]
Zhang, Han-Bing
[1
]
Zhang, Yu-Lu
[1
]
Lu, Yao
[1
]
Meng, Bo
[1
]
Gao, Shan-Shan
[1
]
Huang, Zai-Xing
[1
]
Kang, Guo-Jun
[1
]
Cao, Jing-Pei
[1
,3
]
Wei, Xian-Yong
[1
,3
]
Zhao, Yun-Peng
[1
,3
]
机构:
[1] Key Laboratory of Coal Processing and Efficient Utilization, Ministry of Education, China University of Mining & Technology, Jiangsu, Xuzhou,221116, China
[2] State Key Laboratory of Chemistry and Utilization of Carbon Based Energy Resources, Xinjiang University, Xinjiang, Urumqi,830017, China
[3] Jiangsu Province Engineering Research Center of Fine Utilization of Carbon Resources, China University of Mining & Technology, Jiangsu, Xuzhou,221116, China
来源:
基金:
中国国家自然科学基金;
关键词:
Asphaltenes - Carbon - Catalyst selectivity - Doping (additives) - Fischer-Tropsch synthesis - Hydrocracking - Hydrogen - Hydrogen bonds - Iron compounds - Lignite - Macromolecules - Nitrogen - Phenols;
D O I:
暂无
中图分类号:
学科分类号:
摘要:
Cleaving C-O bridged bonds of lignite via catalytic hydrocracking (CHC) is an effective method to produce chemicals and clean fuels. Herein, a nitrogen-doped carbon supported Fe catalyst was developed by using a one-pot method for CHC of Xilinguole lignite (XL) and its related model compounds. The doped nitrogen enhanced the interaction between Fe and N species to form Fe-N sites and favored forming smaller Fe/Fe3C nanocrystals, which played a crucial role in CHC performance. Toluene and phenol were produced from CHC of benzyl phenyl ether (BPE) with high yield and selectivity at 250 °C over the optimal catalyst with 4% Fe, without hydrogenation products. The Fe-based catalyst activated both H2 and isopropanol to generate hydrogen radicals for cleaving C-O bridged bonds. The CHC of XL under different temperature and time showed that the yields of oil, asphaltene and preasphaltene were obviously promoted under 325 °C, 1 MPa, and 6 h, and they had much higher H/C ratio but remarkably lower O/C ratio, resulting in much higher heating values (28.19–36.90 MJ/kg) than XL. Phenols were the major group component with relative content of 53.6 wt% in oil from CHC, and the asphaltene and preasphaltene from CHC had obviously lower molecular weights, which could attributed to depolymerization of C-O bridged bonds in the XL macromolecular structures over the catalyst. © 2024 Elsevier Ltd
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