Effect of acidic properties of single-crystalline hierarchical ZSM-5 zeolite on its activity and mass transfer in n-heptane catalytic cracking

被引:0
|
作者
Xie X. [1 ]
Zhang X. [1 ]
Liu X. [2 ]
Chong M. [2 ]
Cheng D. [1 ,2 ]
Chen F. [1 ,2 ]
机构
[1] College of Chemical and Biological Engineering, Zhejiang University, Zhejiang, Hangzhou
[2] Institute of Zhejiang University-Quzhou, Zhejiang, Quzhou
关键词
catalysis; L-lysine; mass transfer; reaction; Si/Al ratio; single-crystalline hierarchical ZSM-5 zeolite;
D O I
10.16085/j.issn.1000-6613.2023-2088
中图分类号
学科分类号
摘要
Single-crystalline hierarchical ZSM-5 zeolite with intracrystalline mesopore was successfully synthesized by using L-lysine as a mesoporous template, and the Si/Al ratio was changed by adjusting the adding amount of aluminum source (sodium metaaluminate). Then the effect of acidic properties on zeolite's activity and mass transfer in n-heptane catalytic cracking was investigated in detail. The physical structure, acidic properties and micromorphology of single-crystalline hierarchical ZSM-5 zeolite were characterized by using X-ray diffraction (XRD), nitrogen physical adsorption, ammonia temperature-programmed desorption (NH3-TPD), pyridine infrared (Py-IR), scanning electron microscopy (SEM) and transmission electron microscopy (TEM). In addition, the zero-length column (ZLC) device was employed to test the apparent diffusivity of n-heptane in single-crystalline hierarchical ZSM-5 zeolite, which was used to characterize its mass transfer performance. The results showed that the physical structure of single-crystalline hierarchical ZSM-5 zeolite kept almost the same with the increase of Si/Al ratio, while the zeolite's mass transfer performance was improved with the decrease of acid amount, but the catalytic cracking performance was enhanced with the increase of acid amount. When the Si/Al ratio of the single-crystalline hierarchical ZSM-5 zeolite increased from 80 to 140, the apparent diffusivity of n-heptane could be improved by more than 87%. When the Si/Al ratio was 80, the conversion rate of n-heptane could reach up to 97.5%, and the selectivity of ethylene and propylene were 24.3% and 35.1%, respectively. © 2024 Chemical Industry Press Co., Ltd.. All rights reserved.
引用
收藏
页码:2661 / 2672
页数:11
相关论文
共 47 条
  • [1] BAI Yu'en, ZHANG Binrui, LIU Dongyang, Et al., Influence of synergistic effect of acid properties and pore structure of ZSM-5 zeolite on the catalytic cracking performance of pentene, CIESC Journal, 74, 1, pp. 438-448, (2023)
  • [2] AKAH Aaron, WILLIAMS Jesse, GHRAMI Musaed, An overview of light olefins production via steam enhanced catalytic cracking, Catalysis Surveys from Asia, 23, 4, pp. 265-276, (2019)
  • [3] SHA Yuchen, HAN Lei, WANG Ruoyu, Et al., Tailoring ZSM-5 zeolite through metal incorporation: Toward enhanced light olefins production via catalytic cracking: A minireview, Journal of Industrial and Engineering Chemistry, 126, pp. 36-49, (2023)
  • [4] BLAY Vincent, LOUIS Benoit, MIRAVALLES Ruben, Et al., Engineering zeolites for catalytic cracking to light olefins, ACS Catalysis, 7, 10, pp. 6542-6566, (2017)
  • [5] LI Zhengyu, ZHANG Zhongdong, WANG Gang, Et al., Modified of ZSM-5 zeolites for maximizing light olefins by catalytic pyrolysis, Petrochemical Technology & Application, 39, 6, pp. 462-468, (2021)
  • [6] PAN Xiaoyan, HOU Keke, ZHENG Yifan, Et al., Catalytic performance of n-heptane catalytic cracking of to light olefins over hierarchical ZSM-5 zeolites, Chemical Reaction Engineering and Technology, 38, 1, pp. 23-31, (2022)
  • [7] RAHIMI Nazi, KARIMZADEH Ramin, Catalytic cracking of hydrocarbons over modified ZSM-5 zeolites to produce light olefins: A review, Applied Catalysis A: General, 398, 1, pp. 1-17, (2011)
  • [8] SADRAMELI SM., 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)
  • [9] DEGNAN T F, CHITNIS G K, SCHIPPER P H., History of ZSM-5 fluid catalytic cracking additive development at Mobil, Microporous and Mesoporous Materials, 35, 36, pp. 245-252, (2000)
  • [10] ALIPOUR Shayan Miar, Recent advances in naphtha catalytic cracking by nano ZSM-5: A review, Chinese Journal of Catalysis, 37, 5, pp. 671-680, (2016)