Research and development of hydrocracking catalysts and technologies in China

被引:0
作者
Chong Peng
Yanze Du
Xiang Feng
Yongkang Hu
Xiangchen Fang
机构
[1] SINOPEC,Dalian Research Institute of Petroleum and Petrochemicals
[2] China University of Petroleum,State Key Laboratory of Heavy Oil Processing
来源
Frontiers of Chemical Science and Engineering | 2018年 / 12卷
关键词
hydrocracking; process; catalyst; China;
D O I
暂无
中图分类号
学科分类号
摘要
Hydrocracking of petroleum feedstock represents a compelling route for the production of industrial clean fuels, which has triggered the continuous research and development of core technology related areas such as catalysts, reaction engineering and engineering design. This review particularly focuses on the research and development of catalysts and catalytic processes for hydrocracking of petroleum feedstock in China. Hydroprocessing technologies of China keep pace with the up-todate progress of the world, and some of the technologies have achieved leading role in the world. It is noted that China Petroleum and Chemical Corporation has a full range of hydroprocessing technologies and provides corresponding “tailor-made” catalysts. Through the efforts of several generations, 20 categories of the catalysts including more than 60 brands have been developed, among which more than 40 brands have been successfully applied for more than 130 times. Importantly, the pivotal technical improvements including the deep drawing vacuum gas-oil (VGO) and de-asphalting oil hydrocracking technology to improve material adaptability, the high value-added hydrogenation technology to convert high aromatic diesel conversion to naphtha, the hydrocracking technology using VGO-catalytic diesel blends, the Fushun Research Institute of Petroleum and Petrochemicals’ diesel to gasoline and diesel hydrocracking technologies, and the Sheer hydrocracking technology to reduce energy are reviewed. [graphic not available: see fulltext]
引用
收藏
页码:867 / 877
页数:10
相关论文
共 84 条
[1]  
Tian Z(2009)Research and development of hydroisomerization and hydrocracking catalysts in dalian institute of chemical physics Chinese Journal of Catalysis 30 705-710
[2]  
Liang D(2014)Simulation of an industrial fixed-bed reactor with cocurrent downflow for hydrogenation of pygas Catalysis Today 220-222 237-247
[3]  
Lin L(2014)Hydrocracking of Maya crude oil in a slurry-phase batch reactor II. Effect of catalyst load. Fuel 130 263-272
[4]  
Rojas M(2014)Hydrocracking of Maya crude oil in a slurry-phase reactor. I. Effect of reaction temperature Catalysis Today 220-222 295-300
[5]  
Zeppieri S(2014)Study of waste lubricant hydrocracking into fuel fraction over the combination of Y-Zeolite and ZnO catalyst Procedia Environmental Sciences 20 225-234
[6]  
Ortiz-Moreno H(2011)Prediction of product quality for catalytic hydrocracking of vacuum gas oil Fuel 90 719-727
[7]  
Ramíreza J(2014)Diesel decarbonization via effective catalytic co-hydroprocessing of residual lipids with gas-oil Fuel 136 366-373
[8]  
Sanchez-Minero F(2013)Selective hydrocarbon production by the hydrocracking of glucose Reaction Kinetics, Mechanisms and Catalysis 110 295-307
[9]  
Cuevas R(2013)Hydroprocessing in aqueous phase Industrial & Engineering Chemistry Research 52 17695-17713
[10]  
Ancheyta J(2010)Synergistic process for coker gas oil and heavy cycle oil conversion for maximum light production Industrial & Engineering Chemistry Research 49 11260-11268