中国科学院机构知识库网格
Chinese Academy of Sciences Institutional Repositories Grid
Catalytic Upgrading of in Situ Coal Pyrolysis Tar over Ni-Char Catalyst with Different Additives

文献类型:期刊论文

作者Han, Jiangze1,2; Liu, Xiaoxing1; Yue, Junrong1; Xi, Bingfeng1; Gao, Shiqiu1; Xu, Guangwen1
刊名ENERGY & FUELS
出版日期2014-08-01
卷号28期号:8页码:4934-4941
关键词VOLATILE MATTER SYNTHESIS GAS BROWN-COAL BIOMASS GASIFICATION HYDROCRACKING PERFORMANCE PRESSURE REACTOR
ISSN号0887-0624
其他题名Energy Fuels
中文摘要Ni-char catalyst doped with different additives was used to catalytically upgrade coal pyrolysis tar in situ generated in a laboratory-scale dual-stage reactor. The additives including Fe, Mg, Ce, Zr were all beneficial to the catalytic activity for tar cracking. The best result of tar upgrading was achieved with Ce-Ni-char at a Ce-to-Ni molar ratio of 0.4. The upgrading test at 500 degrees C over a layer of such a catalyst (20% of the tested coal mass) increased the light tar (boiling point <360 degrees C) yield by 10.1%, and the light tar fraction in the tar product to 75 wt % from 52 wt %. The corresponding increase in the molar ratio of H to C of the tar was 61.796. About 60% of the pitch in the original tar from coal pyrolysis was cracked in the catalytic upgrading. The contents of element N and S in the tar after catalytic cracking decreased by 50.5% and 45.8%, respectively. NH3 temperature-programmed desorption results revealed that there were weak Lewis and strong Bronsted acidic sites on the Ni-char catalyst, but many more Lewis acidic sites existed on the Ce-Ni-char catalyst. The addition of Ce into Ni-char facilitated the dispersion of nickel and increased the ability of the catalyst for inhibiting coke deposition.
英文摘要Ni-char catalyst doped with different additives was used to catalytically upgrade coal pyrolysis tar in situ generated in a laboratory-scale dual-stage reactor. The additives including Fe, Mg, Ce, Zr were all beneficial to the catalytic activity for tar cracking. The best result of tar upgrading was achieved with Ce-Ni-char at a Ce-to-Ni molar ratio of 0.4. The upgrading test at 500 degrees C over a layer of such a catalyst (20% of the tested coal mass) increased the light tar (boiling point <360 degrees C) yield by 10.1%, and the light tar fraction in the tar product to 75 wt % from 52 wt %. The corresponding increase in the molar ratio of H to C of the tar was 61.796. About 60% of the pitch in the original tar from coal pyrolysis was cracked in the catalytic upgrading. The contents of element N and S in the tar after catalytic cracking decreased by 50.5% and 45.8%, respectively. NH3 temperature-programmed desorption results revealed that there were weak Lewis and strong Bronsted acidic sites on the Ni-char catalyst, but many more Lewis acidic sites existed on the Ce-Ni-char catalyst. The addition of Ce into Ni-char facilitated the dispersion of nickel and increased the ability of the catalyst for inhibiting coke deposition.
WOS标题词Science & Technology ; Technology
类目[WOS]Energy & Fuels ; Engineering, Chemical
研究领域[WOS]Energy & Fuels ; Engineering
关键词[WOS]VOLATILE MATTER ; SYNTHESIS GAS ; BROWN-COAL ; BIOMASS ; GASIFICATION ; HYDROCRACKING ; PERFORMANCE ; PRESSURE ; REACTOR
收录类别SCI
原文出处://WOS:000340808800011
语种英语
WOS记录号WOS:000340808800011
公开日期2014-09-30
版本出版稿
源URL[http://ir.ipe.ac.cn/handle/122111/11393]  
专题过程工程研究所_研究所(批量导入)
作者单位1.Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, Beijing 100190, Peoples R China
2.Univ Chinese Acad Sci, Beijing 100049, Peoples R China
推荐引用方式
GB/T 7714
Han, Jiangze,Liu, Xiaoxing,Yue, Junrong,et al. Catalytic Upgrading of in Situ Coal Pyrolysis Tar over Ni-Char Catalyst with Different Additives[J]. ENERGY & FUELS,2014,28(8):4934-4941.
APA Han, Jiangze,Liu, Xiaoxing,Yue, Junrong,Xi, Bingfeng,Gao, Shiqiu,&Xu, Guangwen.(2014).Catalytic Upgrading of in Situ Coal Pyrolysis Tar over Ni-Char Catalyst with Different Additives.ENERGY & FUELS,28(8),4934-4941.
MLA Han, Jiangze,et al."Catalytic Upgrading of in Situ Coal Pyrolysis Tar over Ni-Char Catalyst with Different Additives".ENERGY & FUELS 28.8(2014):4934-4941.

入库方式: OAI收割

来源:过程工程研究所

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