Advances in structure design and alkane isomerization performance of metal-zeolite bifunctional catalyst

被引:0
|
作者
Zheng R. [1 ]
机构
[1] Science and Technology Department, China Petroleum & Chemical Corporation, Beijing
关键词
Active site; Catalyst; Diffusion; Isomerization; Precious metals; Zeolite;
D O I
10.16085/j.issn.1000-6613.2021-0330
中图分类号
学科分类号
摘要
Metal-zeolite bifunctional catalysts have two kinds of active sites, which is suitable for promoting the catalytic efficiency of complex reactions such as alkane isomerization. Based on our understanding of the mechanisms of hydrogenation/dehydrogenation on metal sites and carbon chain isomerization on acid sites, several typical cases in frontier researches and the study strategies were summarized in order to provide fundamental insight for the research and development of novel efficient catalysts for alkane isomerization. Regarding the control of the proximity of bifunctional sites, the spatial distribution control strategies of metals, zeolites and binders are introduced, and it is pointed out that the appropriate distance between the two sites is beneficial to the diffusion of olefin intermediates. For improving the utilization of acid sites, the hierarchically structured zeolites with micro-meso porous structure or short diffusion distance are introduced, and it is pointed out that the enhanced diffusion and mass transfer can help to inhibit the side reaction of olefin cracking. To improve the utilization of metal sites, the highly dispersion method of precious metals is introduced, and the strategy of using light transition metals to replace precious metals is briefly described. In view of the future development, it is necessary to further study the proximity of bifunctional sites in the forming process of industrial catalysts, to improve the utilization of acid sites and metal sites, and to reduce the cost of precious metals in catalysts. © 2021, Chemical Industry Press Co., Ltd. All right reserved.
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页码:3785 / 3790
页数:5
相关论文
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  • [1] ANDERSEN M, MEDFORD A J, NORSKOV J K, Et al., Analyzing the case for bifunctional catalysis, Angewandte Chemie: International Edition, 55, 17, pp. 5210-5214, (2016)
  • [2] ZHENG R Y, LIU Z C, WANG Y D, Et al., Industrial catalysis: strategies to enhance selectivity, Chinese Journal of Catalysis, 41, 7, pp. 1032-1038, (2020)
  • [3] TOMASEK S, LONYI F, VALYON J, Et al., Hydrocracking of Fischer-Tropsch paraffin mixtures over strong acid bifunctional catalysts to engine fuels, ACS Omega, 5, 41, pp. 26413-26420, (2020)
  • [4] JAROSZEWSKA K, MASALSKA A, GRZECHOWIAK J R., Hydroisomerization of long-chain bio-derived n-alkanes into monobranched high cetane isomers via a dual-component catalyst bed, Fuel, 268, (2020)
  • [5] JIAO F, LI J, PAN X, Et al., Selective conversion of syngas to light olefins, Science, 351, 6277, pp. 1065-1068, (2016)
  • [6] LIU Yu, TAN Juan, LIU Jing, Et al., Production of bio-jet fuel by hydrocracking and hydroisomerization of long-chain normal bio-paraffins over Pt/ZSM-35 catalysts, Chemical Industry and Engineering Progress, 39, 12, pp. 5086-5094, (2020)
  • [7] XU Tiegang, WU Xianjun, WANG Gang, Et al., Light paraffin isomerizadon catalyst and its development, Chemical Industry and Engineering Progress, 34, 2, pp. 397-401, (2015)
  • [8] GUISNET M., Ideal" bifunctional catalysis over Pt-acid zeolites, Catalysis Today, 218, 219, pp. 123-134, (2013)
  • [9] TAN Y C, HU W J, DU Y Y, Et al., Species and impacts of metal sites over bifunctional catalyst on long chain n-alkane hydroisomerization: a review, Applied Catalysis A: General, 611, (2021)
  • [10] BI Yunfei, XIA Guofu, HUANG Weiguo, Et al., Investigation on the hydroisomerization catalyst-The effect of the hydrogenation function, Acta Petrolei Sinica (Petroleum Processing Section), 34, 1, pp. 64-70, (2018)