Porous Pseudoboehmite as an Active Matrix of Fluid Catalytic Cracking Catalysts: Effects on Pore Structure and Cracking Performance

被引:0
|
作者
Yu, Shanqing [1 ]
Liu, Yuqing [1 ]
Yan, Jiasong [1 ]
Zeng, Shuangqin [1 ]
Zhang, Xuejing [1 ]
Guo, Shuo [1 ]
机构
[1] Sinopec Res Inst Petr Proc Co Ltd, Beijing 100083, Peoples R China
关键词
LIGHT OLEFINS; CRUDE-OIL; CONNECTIVITY; POROSITY; NAPHTHA; ACIDITY; SILICA; BINDER;
D O I
10.1021/acs.iecr.4c04172
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Fluid catalytic cracking (FCC) catalysts rich in meso-macro pores are the main development trend to avoid serious diffusion limitation in the FCC process. This study investigated the pore structure characteristics of two kinds of FCC catalysts (FCC-1 and FCC-2) prepared with different porous pseudoboehmite (PB1 or PB2), especially the effects of size, morphology, and stacking mode of PB1 and PB2 matrix particles on the meso-macro pore structure of catalysts. PB1 in granular or spherical shape tends to stack closely and form smaller interparticle pores centered at 5.7 nm, while PB2 in rod or fibrous shape is more conducive to stack loosely and generate much more abundant larger interparticle pores centered at 12.6 nm. Compared to the PB1-based FCC-1 catalyst with mesopores centered at 4.2 nm, the PB2-based FCC-2 catalyst presents more pores in the 5-100 nm range and larger pore volume based on the N2 adsorption method, the frequency of count for pores at 10-100 nm increasing from 25.8% to 62.0% based on focused ion beam-scanning electron microscopy (FIB-SEM). The 3D pore network analysis of FIB-SEM further calculates the porosity (24.3%), interconnected pores (22.9%), and the ratio of interconnected pores to total pores (94.2%) of the FCC-2 catalyst. The FCC-2 catalyst shows superior heavy oil cracking ability and product selectivity than the FCC-1 catalyst, which could be ascribed to the better diffusion performance of larger meso-macro pores. It provides a new matrix-based approach for constructing FCC catalysts rich in meso-macro pore structures, in addition to in situ crystallization and hierarchical porous zeolites.
引用
收藏
页码:4309 / 4318
页数:10
相关论文
共 50 条
  • [1] PORE STRUCTURE OF CRACKING CATALYSTS
    DOBRES, RM
    RHEAUME, L
    CIAPETTA, FG
    INDUSTRIAL & ENGINEERING CHEMISTRY PRODUCT RESEARCH AND DEVELOPMENT, 1966, 5 (02): : 174 - &
  • [2] Aluminum phosphate as active matrix of fluid catalytic cracking catalysts: Y zeolite stabilization
    de Souza, Eliana Carmo
    Pereira, Marcelo Maciel
    Lam, Yiu Lau
    Morgado Jr, Edisson
    Chinelatto Jr, Luiz Silvino
    APPLIED CATALYSIS A-GENERAL, 2021, 619
  • [3] ROLE OF THE AMORPHOUS MATRIX IN THE HYDROTHERMAL AGING OF FLUID CATALYTIC CRACKING CATALYSTS
    GELIN, P
    COURIERES, TD
    APPLIED CATALYSIS, 1991, 72 (01): : 179 - 192
  • [4] Matrix Effects in a Fluid Catalytic Cracking Catalyst Particle: Influence on Structure, Acidity, and Accessibility
    Velthoen, Marjolein E. Z.
    Paioni, Alessandra Lucini
    Teune, Iris E.
    Baldus, Marc
    Weckhuysen, Bert M.
    CHEMISTRY-A EUROPEAN JOURNAL, 2020, 26 (52) : 11995 - 12009
  • [5] Modification of Kaolinite and Its Effect on the Catalytic Cracking Performance of Fluid Catalytic Cracking
    Rao W.
    Lv G.
    Liao L.
    Kuei Suan Jen Hsueh Pao/Journal of the Chinese Ceramic Society, 2019, 47 (06): : 848 - 854
  • [6] Interactions between heavy metals and clay matrix in fluid catalytic cracking catalysts
    Liu, CH
    Deng, YQ
    Pan, YQ
    Zheng, SG
    Gao, XH
    APPLIED CATALYSIS A-GENERAL, 2004, 257 (02) : 145 - 150
  • [7] Effects of vanadium poisoning on cracking catalysts and development of vanadium-resistant additive for fluid catalytic cracking
    Zheng, Shu-Qin
    Suo, Ji-Shuan
    Zhang, Yong-Ming
    Liu, Hong-Hai
    Duan, Chang-Yan
    Wang, Bao-Jie
    Huagong Xiandai/Modern Chemical Industry, 2002, 22 (02): : 29 - 32
  • [8] Effects of Molecular Structure on Hydrocarbon Catalytic Cracking Performance
    Li, Fuchao
    Yuan, Qimin
    Wei, Xiaoli
    Shiyou Xuebao, Shiyou Jiagong/Acta Petrolei Sinica (Petroleum Processing Section), 2020, 36 (04): : 661 - 666
  • [9] FCC MATRIX EFFECTS ON CATALYTIC CRACKING
    ABNER, DK
    BRADY, MF
    HUMPHRIES, AP
    YANIK, SJ
    ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 1989, 198 : 46 - PETR
  • [10] Performance and characterization of BEA catalysts for catalytic cracking
    Nakao, R
    Kubota, Y
    Katada, N
    Nishiyama, N
    Kunimori, K
    Tomishige, K
    APPLIED CATALYSIS A-GENERAL, 2004, 273 (1-2) : 63 - 73