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《GONGYE CUIHUA (INDUSTRIAL CATALYSIS)》 1995-04
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Kinetic Study of Tetralin Hydrocracking on Mo-Ni Catalyst Containing USY Zeolite

Cao Zubin(Dept Prtrochem Technol, Fushun Petrochem Institute, Fushun, Liaoning, 113001)  
The kinetic data of tetralin hydrocracking reaction on the 3825 catalyst were obtained in a continuous now fixed-bed microreactor at a temperature range of 320 ̄380℃ and a pressure rangs of 4. 5-8.5MPa. The reaction network and kinetic model-for tetralin hydrocracking were thus established.
【Fund】: 中国石化总公司资助
【CateGory Index】: TQ203.2
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【Co-references】
Chinese Journal Full-text Database 10 Hits
1 CAO Zu\|bin\+\{1,2\}, XU Xian\|lun\+\{1*\}, QI Yu\|tai\+2, QI Bang\|feng\+1, LU Shu\|wen\+1 (1. State Key Laboratory of Oxo Synthesis and Selective Oxidation, Lanzhou Institute of Chemical Physics, The Chinese Academy of Sciences, Lanzhou 730000, C;Study on the Kinetics of Tetralin Hydrocracking over Mo-Ni/USY Dual Functional Catalyst[J];Journal of Molecular Catalysis (China);2002-01
2 LI Qing-hua, LIU Yun-qi, LIU Chun-ying, LIU Chen-guang a);Cyclohexane Hydroconversion on Pt/HY-Al_2O_3 Catalysts[J];Journal of Molecular Catalysis;2004-05
3 ZHANG Quan xin,LIU Xi yao (Research Institute of Yanshan Petrochemical Corp,Beijing 102550,China);Hydrocracking of polycyclic aromatic hydrocarbons[J];Gongye Cuihua (Industrial Catalysis);2001-02
4 WANG Dong-hui~(1,2),KONG De-jin~2,Guo Yang-long~1,Qi Xiao-lan~(2),Wang Jun-song~1(1.Researh institute of Industrial Catalyst,East China University of Science and Technology,Shanghai 200237,China;2.Shanghai Research Institute of Petrochemical Technology,SINOPEC,Shanghai 201208,China);Latest researches in processes and catalysts for conversion of heavy aromatics to light one[J];Industrial Catalysis;2005-10
5 YANG Chunliang, DONG Qun, WANG Jian (Department of Chemistry and Chemical Engineering , Daqing Petroleum Institute, Daqing 163318, China );Influencing Factors of Process for Presulfiding Hydrogenation Catalyst[J];Guang Zhou Chemical Industry and Technology;2005-06
6 ZHANG Xiwen1,2,LING Fengxiang2,SUN Wanfu2,FANG Xiangchen,LI Ruifeng1(1 State Key Laboratory of C1 Chemistry and Chemical Technology,Institute of Fine Chemical Technology,Taiyuan University of Science and Technology,Taiyuan 030024;2 Fushun Research Institute of Petroleum and Petrochemicals,SINOPEC,Fushun 113001);Current situation of off-site pre-sulfurizing technique for hydrotreatment catalysts[J];Chemical Industry and Engineering Progress;2006-04
7 ZHOU Zhi-ming,CHENG Zhen-min~*,LI Zhuo,YUAN Wei-kang(UNILAB Research Center of Chemical Reaction Engineering ECUST, Shanghai 200237, China);Reaction Kinetics of Liquid-phase Benzene Hydrogenation on Pd/γ-Al_2O_3[J];Journal of East China University of Science and Technology;2004-01
8 Zhao Xiaohong (Fushun Industrial School 113123) Liu Bingsi Huang Ji (Department of Petrochemical Engineering, Fushun Petroleum Institute 113001);Establishment and Examination of Lumped Model for Tetralin Hydrocracking[J];CHEMICAL INDUSTRY AND ENGINEERING;1997-04
9 Huang Xinlu and Zeng Ronghui(Sinopec Corp.Fushun Research Institute of Petrochemical Technology,Fushun,Liaoning Province 113001,China);New Advances in Hydrocracking Technology[J];Petrochemical Industry Trends;2005-12
10 WANG Lei and QIU Jian guo (Department of Petrochemical Engineering,Fushun Petroleum Institute,Fushun 113001) LI Feng xiao (Petroleum University,Beijing 121001);Study on the Kinetics of Tetralin Hydrocracking Reaction[J];PETROCHEMICAL TECHNOLOGY;1999-04
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