Intrinsic activities and pore diffusion effect in hydrocarbon cracking in steamed Y zeolite

被引:0
|
作者
Kung, HH [1 ]
机构
[1] Northwestern Univ, Dept Chem Engn, Evanston, IL 60208 USA
关键词
D O I
暂无
中图分类号
O61 [无机化学];
学科分类号
070301 ; 081704 ;
摘要
In the literature, it has been shown that the hydrocarbon cracking activity of a zeolite particle can be greatly enhanced by steam treatment. The extent of enhancement depends on the process condition. Recently, it has been shown that under conditions where the reaction is dominated by the monomolecular mechanism, the turnover frequency and the intrinsic activation energy for cracking are practically unchanged by steaming. However, a much larger difference in activity can be observed under conditions where bimolecular and oligomeric cracking dominate. Thus, the phenomenon of enhanced activity by steaming can be explained by the possibility that the bimolecular and oligomeric cracking reactions are pore diffusion-limited. Steaming generates defects in the zeolite particle, increases the external surface area for diffusion, which then leads to the large enhancement in the observed activity.
引用
收藏
页码:23 / 33
页数:11
相关论文
共 44 条
  • [31] Study on secondary pores in zeolite molecular sieve materials II. Effect of intracrystalline secondary pores of Y type zeolite on diffusion
    Bai, Zilong
    Chen, Shaozhou
    Chang, Keyi
    Fu, Yanhong
    Liu, Fuying
    Huadong Huagong Xueyuan Xuebao/Journal of East China Institute of Chemical Technology, 1993, 19 (03): : 249 - 254
  • [32] Effect of hierarchical ZSM-5 zeolite crystal size on diffusion and catalytic performance of n-heptane cracking
    Xu, Shuman
    Zhang, Xiaoxiao
    Cheng, Dangguo
    Chen, Fengqiu
    Ren, Xiaohong
    FRONTIERS OF CHEMICAL SCIENCE AND ENGINEERING, 2018, 12 (04) : 780 - 789
  • [33] Effect of hierarchical ZSM-5 zeolite crystal size on diffusion and catalytic performance of n-heptane cracking
    Shuman Xu
    Xiaoxiao Zhang
    Dang-guo Cheng
    Fengqiu Chen
    Xiaohong Ren
    Frontiers of Chemical Science and Engineering, 2018, 12 : 780 - 789
  • [34] Green synthesis and performance of micro-mesoporous ZSM-5/Y composite zeolite with hierarchical pore structure for vacuum gas oil (VGO) catalytic cracking
    Wang, Fei
    Xie, Yaxuan
    Liu, Yuxiang
    Lyu, Yuchao
    Fu, Jianye
    Ma, Lishuang
    Liu, Xinmei
    CHEMICAL ENGINEERING JOURNAL, 2025, 506
  • [35] Catalytic Cracking of Hydrocarbons in a CREC Riser Simulator Using a Y-Zeolite-Based Catalyst: Assessing the Catalyst/Oil Ratio Effect
    Alkhlel, A.
    de Lasa, H.
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2018, 57 (41) : 13627 - 13638
  • [36] Hydrocracking activity and selectivity of VGO .1. Effect of metal loading to Y-zeolite for the catalytic activities.
    Isoda, T
    Kusakabe, K
    Morooka, S
    ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 1997, 213 : 91 - PETR
  • [37] COUNTERDIFFUSION OF LIQUID HYDROCARBONS IN TYPE-Y ZEOLITE - EFFECT OF MOLECULAR-SIZE, MOLECULAR TYPE, AND DIRECTION OF DIFFUSION
    MOORE, RM
    KATZER, JR
    AICHE JOURNAL, 1972, 18 (04) : 816 - &
  • [38] PROMOTIVE EFFECT OF HYDROGEN-SULFIDE ON THE CATALYTIC ACTIVITIES OF METAL-IONS EXCHANGED Y-ZEOLITES FOR CUMENE CRACKING
    HOSOTSUBO, T
    SUGIOKA, M
    SANADA, Y
    AOMURA, K
    NIPPON KAGAKU KAISHI, 1979, (01) : 28 - 32
  • [39] Mass diffusion effect in large zeolite Y aggregates on Pd cluster size distribution:: A combined in situ EXAFS/XRD study
    Vogel, W
    Knözinger, H
    Carvill, BT
    Sachtler, WMH
    Zhang, ZC
    JOURNAL OF PHYSICAL CHEMISTRY B, 1998, 102 (10): : 1750 - 1758