中国科学院机构知识库网格
Chinese Academy of Sciences Institutional Repositories Grid
Detailed Description of Coal Tar Hydrogenation Process Using the Kinetic Lumping Approach

文献类型:期刊论文

作者Dai, Fei1,2; Gao, Mingjie1; Li, Chunshan1; Xiang, Shuguang2; Zhang, Suojiang2
刊名ENERGY & FUELS
出版日期2011-11-01
卷号25期号:11页码:4878-4885
关键词heavy oil hydrocracking model liquefaction pyrolysis catalyst residue gasoline
ISSN号0887-0624
其他题名Energy Fuels
中文摘要A new eight-lump kinetic model containing 19 kinetic constants is proposed to describe coal tar hydrogenation. The model contains lump 1 (> 300 degrees C), lump 2 (250-300 degrees C), lump 3 (200-250 degrees C), lump 4 (20-200 degrees C), diesel, gasoline, gas, and coke as lumps. The kinetic parameters were determined using least-squares regression analysis of the experimental data, obtained in two-stage fixed beds filled with the laboratory-made catalysts at various operating conditions. The proposed model was also validated. Comparisons between the experimental data and predictions using the lumping kinetic model showed good agreement. The variation in product yields and product distribution with operating conditions and feed properties was predicted. The effects of space velocity, hydrogen/oil ratio, temperature, initial hydrogen pressure, and other reaction conditions on hydrogenation performance were also investigated.
英文摘要A new eight-lump kinetic model containing 19 kinetic constants is proposed to describe coal tar hydrogenation. The model contains lump 1 (> 300 degrees C), lump 2 (250-300 degrees C), lump 3 (200-250 degrees C), lump 4 (20-200 degrees C), diesel, gasoline, gas, and coke as lumps. The kinetic parameters were determined using least-squares regression analysis of the experimental data, obtained in two-stage fixed beds filled with the laboratory-made catalysts at various operating conditions. The proposed model was also validated. Comparisons between the experimental data and predictions using the lumping kinetic model showed good agreement. The variation in product yields and product distribution with operating conditions and feed properties was predicted. The effects of space velocity, hydrogen/oil ratio, temperature, initial hydrogen pressure, and other reaction conditions on hydrogenation performance were also investigated.
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]HEAVY OIL ; HYDROCRACKING ; MODEL ; LIQUEFACTION ; PYROLYSIS ; CATALYST ; RESIDUE ; GASOLINE
收录类别SCI
原文出处://WOS:000297001400002
语种英语
WOS记录号WOS:000297001400002
公开日期2013-11-28
版本出版稿
源URL[http://ir.ipe.ac.cn/handle/122111/6302]  
专题过程工程研究所_研究所(批量导入)
作者单位1.Chinese Acad Sci, State Key Lab Multiphase Complex Syst, Inst Proc Engn, Beijing 100190, Peoples R China
2.Qingdao Univ Sci, Hitech Inst Petr, Qingdao 266042, Shandong, Peoples R China
推荐引用方式
GB/T 7714
Dai, Fei,Gao, Mingjie,Li, Chunshan,et al. Detailed Description of Coal Tar Hydrogenation Process Using the Kinetic Lumping Approach[J]. ENERGY & FUELS,2011,25(11):4878-4885.
APA Dai, Fei,Gao, Mingjie,Li, Chunshan,Xiang, Shuguang,&Zhang, Suojiang.(2011).Detailed Description of Coal Tar Hydrogenation Process Using the Kinetic Lumping Approach.ENERGY & FUELS,25(11),4878-4885.
MLA Dai, Fei,et al."Detailed Description of Coal Tar Hydrogenation Process Using the Kinetic Lumping Approach".ENERGY & FUELS 25.11(2011):4878-4885.

入库方式: OAI收割

来源:过程工程研究所

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