Preparation and property of low coke yield resid catalytic cracking catalyst

被引:0
作者
Zhang, JM [1 ]
Wang, XP
Xie, P
Li, MZ
Zhang, JL
Yang, Y
Liu, ZM
机构
[1] Dalian Univ Technol, State Key Lab Fine Chem, Dalian 116024, Liaoning, Peoples R China
[2] Chinese Acad Sci, Dalian Inst Chem Phys, Dalian 116023, Liaoning, Peoples R China
关键词
resid; catalytic cracking; ultrastable Y zeolite; coke yield; silica-alumina ratio;
D O I
暂无
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
A series of ultrastable Y zeolite samples (FSY) with high Si/Al ratio were prepared. The acid site amount of FSY samples could be effectively adjusted by dealumination with (NH4)(2)SiF6 and hydrothermal treatment. Therefore, the FSY sample with a suitable amount of acid sites and definite acidity could be expected. After being modified by lanthanum, the LaFSY zeolite with more strong acid sites and less weak acid sites was obtained, and it showed a high activity and gave a low coke yield in resid fluid catalytic cracking (RFCC). After being aged in 100 % water vapor at 800 degrees C for 17 h, the catalyst with the LaFSY zeolite as the active component gave a total liquid yield of 88.9% and coke yield of 7.5% in the RFCC reaction of Daqing resid. Compared with another generally used industrial catalyst that gave a total liquid yield of 85.4% and coke yield of 9.0%, the LaFSY catalyst could be considered as a better catalyst for RFCC.
引用
收藏
页码:1053 / 1058
页数:6
相关论文
共 37 条
  • [1] INFLUENCE OF FRAMEWORK ALUMINUM GRADIENTS ON THE CATALYTIC ACTIVITY OF Y-ZEOLITES - CRACKING OF GAS-OIL ON Y-ZEOLITES DEALUMINATED BY DIFFERENT PROCEDURES
    ARRIBAS, J
    CORMA, A
    FORNES, V
    MELO, F
    [J]. JOURNAL OF CATALYSIS, 1987, 108 (01) : 135 - 142
  • [2] Beyer H. K., 1980, STUDIES SURFACE SCI, V5, P203, DOI DOI 10.1016/S0167-2991(08)64880-6
  • [3] PREPARATION OF HIGH-SILICA FAUJASITES BY TREATMENT WITH SILICON TETRACHLORIDE
    BEYER, HK
    BELENYKAJA, IM
    HANGE, F
    TIELEN, M
    GROBET, PJ
    JACOBS, PA
    [J]. JOURNAL OF THE CHEMICAL SOCIETY-FARADAY TRANSACTIONS I, 1985, 81 : 2889 - 2901
  • [4] Breck D. W., 1985, US Pat, Patent No. [4503023, 4503023A]
  • [5] CHEN YL, 1997, PETROL PROCESS PETRO, V28, P22
  • [6] Hydrogen transfer, coke formation, and catalyst decay and their role in the chain mechanism of catalytic cracking
    Cumming, KA
    Wojciechowski, BW
    [J]. CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 1996, 38 (01): : 101 - 157
  • [7] Study on the formation of mesopore during hydrothermal dealumination of Y zeolite
    Dong, ST
    Li, XW
    Li, DD
    Shi, YH
    Nie, H
    Kang, XH
    [J]. ACTA PHYSICO-CHIMICA SINICA, 2002, 18 (03) : 201 - 206
  • [8] DETERMINATION OF INTEGRATED MOLAR EXTINCTION COEFFICIENTS FOR INFRARED-ABSORPTION BANDS OF PYRIDINE ADSORBED ON SOLID ACID CATALYSTS
    EMEIS, CA
    [J]. JOURNAL OF CATALYSIS, 1993, 141 (02) : 347 - 354
  • [9] HYDROTHERMAL DEALUMINATION OF FAUJASITES
    FLEISCH, TH
    MEYERS, BL
    RAY, GJ
    HALL, JB
    MARSHALL, CL
    [J]. JOURNAL OF CATALYSIS, 1986, 99 (01) : 117 - 125
  • [10] GAO Z, 1990, ACTA CHIM SINICA, V48, P632