Zeolite catalysts for catalytic cracking of hydrocarbon to increase light olefins selectivity

被引:0
|
作者
Liu Q. [1 ]
Chen Z. [1 ]
Piao Y. [1 ]
Xiao P. [1 ]
Ge Y. [1 ]
Gong Y. [1 ]
机构
[1] State Key Laboratory of Heavy Oil Processing, Key Laboratory of Catalysis of CNPC, College of Chemical Engineering and Environment, China University of Petroleum, Beijing
来源
Huagong Xuebao/CIESC Journal | 2024年 / 75卷 / 01期
关键词
catalysis; light olefin; molecular sieves; performance regulation; selectivity; ZSM-5;
D O I
10.11949/0438-1157.20230845
中图分类号
学科分类号
摘要
Light olefins such as ethylene and propylene are the most important basic raw materials in the chemical industry. In recent years, the global demand for light olefins has continued to increase, and the development of technology to increase the production of light olefins through catalytic cracking of different raw materials will remain the main direction. In this work, we focus on the efficient production of light olefins by catalytic cracking process and the research progress in the preparation and catalytic cracking performance of zeolite catalysts, especially in the synthesis and performance modulation mainly based on ZSM-5 zeolites is reviewed. For the increase of production of light olefins, ZSM-5 zeolites by using diversified synthesis method are provided, its modulation of texture and acid properties of ZSM-5 zeolites by modification with different elements, preparation of hierarchical porous structures are introduced, and the effects on feedstock conversion, light olefins selectivity and catalyst stability are emphatically discussed. The structure-activity relationship of catalytic cracking over the ZSM-5 catalysts to increase the production of light olefins is summarized and elucidated. Finally, the new ways for improving the regulation of light olefin distribution by precisely regulating ZSM-5 zeolites is further prospected, which lays the foundation for designing key catalysts for catalytic cracking hydrocarbons to produce light olefins. © 2024 Materials China. All rights reserved.
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页码:120 / 137
页数:17
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共 110 条
  • [1] Meng X H, Gao J S, Li L, Et al., Advances in catalytic pyrolysis of hydrocarbons, Petroleum Science and Technology, 22, 9, pp. 1327-1341, (2004)
  • [2] Sadrameli S M., Thermal/catalytic cracking of liquid hydrocarbons for the production of olefins: a state-of-the-art review (Ⅱ): Catalytic cracking review, Fuel, 173, pp. 285-297, (2016)
  • [3] Wang H H, Sun L Y, Xing L F, Et al., Transformation of light hydrocarbons to olefins: effect of ZSM-5 zeolites crystal size, CIESC Journal, 66, 10, pp. 3940-3949, (2015)
  • [4] Tang X Y, Wang S J, Xiao M, Et al., Research progress in heavy oil catalytic pyrolysis technology for light olefins and its catalysts, Contemporary Chemical Industry, 49, 4, pp. 620-625, (2020)
  • [5] Auepattana-Aumrung C, Suriye K, Jongsomjit B, Et al., Inhibition effect of Na<sup>+</sup> form in ZSM-5 zeolite on hydrogen transfer reaction via 1-butene cracking, Catalysis Today, 358, pp. 237-245, (2020)
  • [6] Peng P, Gao X H, Yan Z F, Et al., Diffusion and catalyst efficiency in hierarchical zeolite catalysts, National Science Review, 7, 11, pp. 1726-1742, (2020)
  • [7] Xie Z K, Liu Z C, Wang Y D, Et al., Applied catalysis for sustainable development of chemical industry in China, National Science Review, 2, 2, pp. 167-182, (2015)
  • [8] Cnudde P, de Wispelaere K, van der Mynsbrugge J, Et al., Effect of temperature and branching on the nature and stability of alkene cracking intermediates in H-ZSM-5, Journal of Catalysis, 345, pp. 53-69, (2017)
  • [9] Zhang Y, Shen K X, Teng J W., Review of the olefin catalytic cracking technology, Chemical Reaction Engineering and Technology, 37, 2, pp. 181-192, (2021)
  • [10] Liu X L, Shi J, Yang G, Et al., A diffusion anisotropy descriptor links morphology effects of H-ZSM-5 zeolites to their catalytic cracking performance, Communications Chemistry, 4, (2021)