KINETICS OF GAS-OIL CRACKING AND CATALYST DECAY ON SAPO-37 AND USY MOLECULAR-SIEVES

被引:18
作者
CORMA, A
MARTINEZTRIGUERO, J
机构
[1] Institute de Tecnología Química, UPV-CSIC, Universidad Politécnica de Valencia
关键词
CATALYTIC CRACKING; DEACTIVATION; GAS-OIL CRACKING; KINETICS; SAPO-37; USY;
D O I
10.1016/0926-860X(94)80310-2
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
A kinetic study of gasoil cracking has been carried out on USY and SAPO-37 catalysts. In the MAT experiment USY gives a lower cumulative average conversion, its intrinsic activity is higher, but it decays much faster than SAPO-37. This behavior is discussed on the basis of acidity distribution in the catalysts. Because of the differences in hydrogen transfer activity, the order of cracking for USY and SAPO-37 is different, too. Simulation results indicate that, in a commercial FCC unit, a higher conversion should be expected for USY, as long as the contact time is less than or equal to 3.
引用
收藏
页码:153 / 162
页数:10
相关论文
共 14 条
  • [1] RECENT PROCESS-RELATED AND CATALYST-RELATED DEVELOPMENTS IN FLUID CATALYTIC CRACKING
    BISWAS, J
    MAXWELL, IE
    [J]. APPLIED CATALYSIS, 1990, 63 (02): : 197 - 258
  • [2] CORMA A, 1988, ACS SYM SER, V368, P542
  • [3] CORMA A, 1991, ACS SYM SER, V452, P79
  • [4] CORMA A, 1992, 9TH P INT C ZEOL, V2, P343
  • [5] CORMA A, 1990, Patent No. 2011993
  • [6] DESALDARRIAGA LS, 1987, J AM CHEM SOC, V109, P2686
  • [7] DESALDARRIAGA LS, 1992, J AM CHEM SOC, V2, P343
  • [8] Edwards G.C., 1987, US Patent, Patent No. [4,681,864, 4681864]
  • [9] HABIB ET, 1990, HYDROCARBON CHEMISTRY OF FCC NAPHTHA FORMATION, P1
  • [10] Lok B.M., 1984, US Patent, Patent No. [4,440,871, 4440871, 4440,871]