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《Chemical Engineering of Oil and Gas》 2003-04
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STUDY OF PRODUCING THE GASOLINE WITH LOWER OLEFIN CONTENT BY FCC TECHNOLOGY

Mao Anguo (Research Institute of Petroleum Processing) . CHEMICAL ENGINEERING OF OIL & GAS, VOL. 32, NO.4, PP219 - 221, 2003 ( ISSN 1007 - 3426, IN CHINESE)  
New gasoline standard that the olefin content in the gasoline is not greater than 35% (9) has been executed in China since 1/7/2003. It makes FCC process and technology to face the new challenges and developing chances. By means of choosing suitable catalysts and optimizing the operation parameters, the hydrogen transfer and i-somerization reactions can be intensified under the condition of meeting the heavy oil conversion, and the gasoline with lower olefin content and higher octane number can be obtained from the commercial FCCU.
【CateGory Index】: TE626
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【References】
Chinese Journal Full-text Database 7 Hits
1 YOU Hongjun~(1,2),XU Chunming~2,GAO Jinsen~2(1.Liaoning University of Petroleum & Chemical Technology,Fushun 113001,Liaoning,China;2.State Key Laboratory of Heavy Oil Processing,University of Petroleum,Beijing 102249,China);Effects of reaction temperature on aromatization of FCC gasoline[J];Industrial Catalysis;2006-12
2 YOU Hong-jun ( Petrochemical Faculty, Liaoning University of Petroleum & Chemical Technology, Liaoning Fushun 113001, China );Effects of Reaction Temperature on the Aromatization Reaction of FCC Gasoline[J];Journal of Hebei University of Technology;2006-06
3 YOU Hong-jun(Key Laboratory of Heavy Oil Processing in China,Liaoning University of Petroleum and Chemical Technology,Fushun Liao-2ning 113001,China);Effects of weight ratio of catalyst to oil and weight ratio of water to oil on aromatization reaction of FCC gasoline[J];Hebei Journal of Industrial Science and Technology;2007-02
4 YOU Hong-jun,XU Chun-ming,GAO Jin-sen(State Key Laboratory of Heavy Oil Processing,University of Petroleum,Beijing 102249 PRC);Effects of Reaction Temperature on the Aromatization Reaction of FCC Gasoline[J];Jiangxi Science;2006-04
5 YOU Hong-jun,XU Chun-ming,GAO Jin-sen (State Key Laboratory of Heavy Oil Processing,China University of Petroleum,Beijing 102249,P.R.China);Effects of Weight Hour Space Velocity on the Aromatization Reaction of FCC Gasoline[J];Journal of Petrochemical Universities;2006-01
6 Liang Yongmei,Jia Yongxia,Gao Jinsen (State Key Laboratory of Heavy Oil Processing,China University of Petroleum,Beijing 102249);INFLUENCE OF LBO-A ADDITIVE DOSAGE ON THE CATALYTIC CRACKING REACTIONS OF DAQING ATMOSPHERIC RESIDUE[J];Petroleum Processing and Petrochemicals;2009-12
7 YOU Hong-jun(College of Chemistry and Chemical Engineering,Liaoning University of Petroleum & Chemical Technology,Fushun 113001,Liaoning,China);Effect of reaction temperature on the product of aromatization reaction of FCC gasoline narrow fraction[J];Journal of Xi'an Shiyou University(Natural Science Edition);2007-01
【Citations】
Chinese Journal Full-text Database 2 Hits
1 Gao Liang Dong Xiaoli(Linyuan Refinery, Daqing 163813) Jin Wenlin(Research Institute of Petroleum Processing);STUDY ON SPENT CATALYST STRIPPING IN FCC FAMILY TECHNOLOGIES[J];PETROLEUM PROCESSING AND PETROCHEMICALS;1999-11
2 Zhang Linghul; Cao Ping; Shi Zhicheng; Shi Wenyuan; Li Zaiting(Research Institute of Petroleum Processtng, Beijing 100083);THE INFLUENCE OF CATALYTIC CRACKING TEMPERATURE ON THE SELECTIVITY OF ISOBUTYLENE[J];PETROLEUM PROCESSING AND PETROCHEMICALS;1996-02
【Co-citations】
Chinese Journal Full-text Database 10 Hits
1 MA Hong-chao,CHU Ting-ting,FU Ying-huan,DONG Xiao-li,XUE Wen-pingSchool of Chemistry Engineering & Material,Dalian Polytechnic University,Dalian 116034,China;Preparation of V-Al-O catalysts by hydrothermal route and their isobutane dehydrogenation performance[J];Journal of Dalian Polytechnic University;2010-03
2 ZHANG Yong-min, LU Chun-xi, SHI Ming-xian (University of Petroleum, Beijing 102249, China);Study on the Gas-Solid Mass Transfer Performance in Catalyst Stripper[J];Journal of Chemical Engineering of Chinese Universities;2004-04
3 Mao Anguo,Chang Xueliang,Gu Jie(Research Institute of Petroleum Processing,SINOPEC ,Beijing 100083,China);Analysis of applying quench technology in FCCU[J];Pebrochemical Technology & Application;2003-04
4 Li Peng1,Liu Mengxi1,Han Shouzhi2,Lu Chunxi1(1.State Key Laboratory of Heavy Oil Processing,China University of Petroleum(Beijing),Beijing 102249,China;2.Yangzi Refinery,Yangzi Petrochemical Company,SINOPEC,Nanjing 210048,China);Commercialization of disc and donut-airlift loop hybrid stripper in fluidized-bed catalytic cracking unit of Yangzi Petrochemical Company[J];Petrochemical Technology & Application;2009-01
5 Yu Haiming You Kewei Qingdao Petrochemical Co.,Ltd.,SINOPEC (Qingdao 266043,Shandong,China);REVAMP OF STRIPPER OF HEAVY OIL FCC UNIT[J];Petroleum Refinery Engineering;2008-02
6 Zhang Yongmin.The National Major Lab of Heavy Oil Research of China Petroleum University,P.C.102249;ACTUALITIES AND PROSPECTING OF FCC STRIPPING TECHNOLOGY[J];Petro-Chemical Equipment Technology;2006-02
7 Li Zaiting,Jiang Fukang,Xie Chaogang and Xu Youhao (SINOPEC Research Institute of Petroleum Processing,Beijing 100083,China);DCC Technology and Its Commercial Experience[J];Petrochemical Industry Trends;2001-10
8 Xie Chaogang(Research Institute of Petroleum Processing,Beijing 100083);Commercial Application of Deep Catalytic Cracking Catalysts for Production of Light Olefins[J];PETROCHEMICAL TECHNOLOGY;1997-12
9 YU Guo-qing, GAO Jin-sen, XU Chun-ming (The State Key Laboratory of Heavy Oil Processing, University of Petroleum, Beijng 102249, China);Development of the Stripper and the Stripping Techniques of RFCC Units[J];Shenyang Chemical Industry;2004-02
10 Lan Xingying,Xu Chunming,Yu Guoqing,Gao Jinsen (State Key Laboratory of Heavy Oil Processing,China University of Petroleum,Beijing 102249);STUDY OF ON-LINE SAMPLING AT COMMERCIAL RFCC STRIPPER[J];Petroleum Processing and Petrochemicals;2007-08
【Co-references】
Chinese Journal Full-text Database 10 Hits
1 Chen Xinguo Xu Chunming Chen Zhongbao (1 Oil & Gas Development Co. , CNOOC, Beijing 100027; 2 State Key Laboratory of Heavy Oil Processing, University of Petroleum , Beijing 102249);Study on Catalytic Cracking Rules of Daqing Residue[J];Journal of Beijing Institufe of Petrochemical Technology;2003-03
2 FENG Cui-lan 1, CAO Zu-bin 1,2 , XU Xian-lun 2, BAN Hong-yan 1, GONG Wang-xin 1(1. Petrochemical Engineering Faculty, Fushun Petroleum Institute,Liaoning Fushun 113001,China;2. Chinese Academy of Sciences, Lanzhou Institute of Chemical Physics, Ga;The Technology Trogress in Decreasing Olefins of FCC Gasoline[J];Journal of Fushun Petroleum Institute;2002-02
3 LIU Jun-hua 1 , Xiao Li 1,2 , CAO Zu-bin 1* , YANG Hua 1 (1. Petrochemical College of Liaoning University of Petroleum & Chemical Technology, Fushun 113001, China; 2. Chemical College, China University of Science and Technology, Shanghai 200237, China);The Research of Reducing-olefin Technology of FCC Gasoline on the Ni-Mo-P/USY Catalyst[J];Journal of Molecular Catalysis;2006-02
4 ZOU Xubiao, QIN Song, MAO Xuewen(The Catalyst Works of PetroChina Lanzhou Petrochemical Corporation, Gansu, Lanzhou 730060, China);Development and application of LGO series olefin-reducing RFCC catalyst[J];Gongye Cuihua (Industrial Catalysis);2003-01
5 YOU Hong-jun(Key Laboratory of Heavy Oil Processing in China,Liaoning University of Petroleum and Chemical Technology,Fushun Liao-2ning 113001,China);Effects of weight ratio of catalyst to oil and weight ratio of water to oil on aromatization reaction of FCC gasoline[J];Hebei Journal of Industrial Science and Technology;2007-02
6 Xu Tao~1 Wang Peng~2 (1.Sinopec Management Dept.of Production and Operation,Beijing 100029; 2.Sinopec Qingdao Petrochemical Plant,Qingdao Shandong 266043 China);Feasibility of Processing HA Oil under High Oil Price[J];Journal of Sinopec Management Institute;2006-02
7 Lu Xiaoping, Han Pingfang(Department of Chemical Engineering, Nanjing University of Chemical Technology, Nanjing, 210009);Technical Development of the Removal of Naphthenic Acid from Heavy Sour Crude and Its Fraction[J];Chemical Industry and Engineering Progress;1999-04
8 Fu Xiaoqin 1,2 ,Tian Songbai1, Hou Suandi1 ,Wang Xieqing1(1 Research Intitute of Petroleum Processing , Beijing 100083; 2 Technical Center of Zhenghai Refining & Chemical Company , Ningbo 315207);Development of Catalytic Decarboxylation of Highly Sour Crude Oil[J];Chemical Industry and Engineering Progress;2005-09
9 Wei Fei;Liu Jinzhong;Jin Yong(Department of Chemical Engineering,Tsinghua University,Beijing 100084);HYDRODYNAMICS AND MIXING BEHAVIOUR IN ENTRANCE OF DOWNER[J];Journal of Chemical Industry and Engineering(China);1998-01
10 Cheng Yi,Wei Fei,Zheng Yu and Jin Yong Guo Yincheng and Lin Wenyi (Department of Chemical Engineering, (Department of Engineering Mechanics, Tsinghua University, Beijing?100084) Ts;COMPUTATIONAL FLUID DYNAMIC MODELING OF HYDRODYNAMICS IN DOWNER REACTORS[J];JOURNAL OF CHEMICAL INDUSTRY AND ENGINEERING(CHINA);2000-03
【Secondary References】
Chinese Journal Full-text Database 4 Hits
1 YOU Hong-jun(College of Chemical Engineering,Liaoning University of Petrolem and Chenical Technology,Fushun 113001,China);Effects of Reaction Temperature on the Aromatization Reaction of Huabei C4 Liquefied Petroleum Gas[J];Journal of Guangdong University of Technology;2007-01
2 YOU Hong-jun(Key Laboratory of Heavy Oil Processing in China,Liaoning University of Petroleum and Chemical Technology,Fushun Liao-2ning 113001,China);Effects of weight ratio of catalyst to oil and weight ratio of water to oil on aromatization reaction of FCC gasoline[J];Hebei Journal of Industrial Science and Technology;2007-02
3 Gao Yongfu,Fan Jiangtao,Wang Zhifeng,Zeng Lingzhi,Gao Xionghou (Lanzhou Petrochemical Research Center,PetroChina,Lanzhou 730060,China);Aromatization of catalytic cracking of gasoline on LBO-A and LBO-16 catalyst[J];Petrochemical Technology & Application;2007-06
4 SHA Youxin,LONG Jun,XIE Chaogang,LI Zheng,Yuan Qimin(Research Institute of Petroleum Processing,SINOPEC,Beijing 100083,China);EFFECT OF OPERATING PARAMETERS ON THE FORMATION OF PROPYLENE IN THE GASOLINE CATALYTIC CRACKING REACTION AND ITS REASONS[J];Acta Petrolei Sinica(Petroleum Processing Section);2010-S1
China Proceedings of conference Full-text Database 1 Hits
1 SHA Youxin,LONG Jun,XIE Chaogang,LI Zheng,Yuan Qimin (Research Institute of Petroleum Processing,SINOPEC,Beijing,100083,China);EFFECT OF OPERATING PARAMETERS ON THE FORMATION OF PROPYLENE IN THE GASOLINE CATALYTIC CRACKING REACTION AND ITS REASONS[A];[C];2010
【Secondary Citations】
Chinese Journal Full-text Database 4 Hits
1 Li Zaiting Min Enze Jiang Fukang Wang Xieqing (Reseach Institute of Petroluem Processing);DEEP CATALYTIC CRACKING(DCC)FOR GASEOUS OLEFIN PRODUCTION[J];Petroleum Processing and Petrochemicals;1989-07
2 Huo Yongqing;Wang Yamin;Wang Xieqing;Chen Zubi;Fang Jicai;Xu Shitai Research Institute of Petroleum Processing, Beijing Lanzhou Petroleum Processing & Chemical Compler. SINOPEC;A NOVEL CATALYTIC CONVERSION PROCESS FOR MAXIMUM LPG PLUS GASOLINE PRODUCTION(MGG)[J];Petroleum Processing and Petrochemicals;1993-05
3 Zhong Lexin;Huo Yongqing(Research Institute of Petroleum Processing, Beijing 100083)Wang Junhua;Lu Yan(Yangzi Petrocheminal Works);ARGG PROCESS FOR MAXIMUM GAS PLUS GASOLINE PRODUCTION FROM ATMOSPHERIC RESIDUE[J];PETROLEUM PROCESSING AND PETROCHEMICALS;1995-06
4 Zhang Linghui; Li Zaiting;Xu Youhao(Research Institute of Petroleum Processing,Beijing 100083);THE DIFFERENCE OF CRACKING REACTION BETWEEN ZSM-5 ZEOLITE CATALYSTS WITH DIFFERENT CRYSTAL SIZES[J];PETROLEUM PROCESSING AND PETROCHEMICALS;1995-10
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