Fe-Al isomorphous and self-pillared ZSM-5 nanosheet catalyst for cracking of n-heptane with enhanced selectivity of light olefins

被引:15
作者
Xia, Song [1 ]
Zhu, Yulin [1 ]
Tian, Yajie [1 ,3 ]
He, Xinyu [1 ]
Guo, Longhui [1 ]
Qiao, Congzhen [1 ]
Liu, Guozhu [2 ,3 ]
机构
[1] Henan Univ, Coll Chem & Chem Engn, Henan Prov Engn Res Ctr Catalyt React, Green Energy & Mat Int Joint Lab, Kaifeng 475004, Henan, Peoples R China
[2] Tianjin Univ, Sch Chem Engn & Technol, Key Lab Green Chem Technol, Minist Educ, Tianjin 300072, Peoples R China
[3] Haihe Lab Sustainable Chem Transformat, Tianjin 300192, Peoples R China
基金
中国国家自然科学基金;
关键词
Catalytic cracking; Self-pillared nanosheet; Light olefins; Fe-Al isomorphous; MFI ZEOLITE NANOSHEETS; OLEIC-ACID; HIERARCHICAL ZSM-5; C-5; RAFFINATE; HZSM-5; PERFORMANCE; ETHYLENE; UNIT; NANOPARTICLES; HYDROCARBONS;
D O I
10.1016/j.joei.2022.03.008
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Series Fe-Al isomorphous and self-pillared ZSM-5 nanosheets zeolite (Al-Fe-SPZ) with different Fe/Al molar ratios were synthesized by one-pot strategy for catalytic cracking of n-heptane to produce light olefins. All the Al-Fe-SPZ catalysts gave high surface areas and pore volumes, ascribing to the intersection of nanosheet layers. The addition of Fe in zeolite framework resulted in the decrease of surface acid concentrations (especially the strong acid concentrations). The effect of Fe modification on olefins selectivity in catalytic cracking reaction had two sides. On one hand, reducing the amount of acid, helped to inhibit the hydride transfer, cyclization and aromatic cyclization of olefins in the product at adjacent Bronsted acid sites. However, the reduced acid concentrations led to the decrease of the cracking depth, and the cracking of intermediate products (C-4 and C-5) was inhibited, thus giving a decreased olefin selectivity. With Si/(Al+Fe) molar ratio of 100 and Al/Fe ratio of 84/16, Al-Fe-SPZ catalyst gave the highest yield of light olefins (44.8 wt% of ethylene and propylene) in cracking of n-heptane. In addition, Fe modified zeolite catalyst show excellent cracking stability with low coke deposition.
引用
收藏
页码:196 / 205
页数:10
相关论文
共 67 条
[61]   Radical induced cracking of naphtha model compound: Using bibenzyl as a novel radical initiator [J].
Zhang, Xurui ;
Chen, Zezhou ;
Liu, Zhenyu ;
Liu, Qingya .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2021, 156
[62]   Alkali-treatment of ZSM-5 zeolites with different SiO2/Al2O3 ratios and light olefin production by heavy oil cracking [J].
Zhao, Liang ;
Gao, Jinsen ;
Xu, Chunming ;
Shen, Baojian .
FUEL PROCESSING TECHNOLOGY, 2011, 92 (03) :414-420
[63]   Synthesis of mesoporous ZSM-5 zeolites and catalytic cracking of ethanol and oleic acid into light olefins [J].
Zhao, Tingting ;
Li, Fuwei ;
Yu, Hongchang ;
Ding, Shilei ;
Li, Zhixia ;
Huang, Xinyuan ;
Li, Xiang ;
Wei, Xiaohan ;
Wang, Zhenlin ;
Lin, Hongfei .
APPLIED CATALYSIS A-GENERAL, 2019, 575 :101-110
[64]   Light Olefin Synthesis from Syngas over Sulfide-Zeolite Composite Catalyst [J].
Zhou, Haibo ;
Liu, Su ;
Su, Junjie ;
Liu, Chang ;
Zhang, Lin ;
Jiao, Wenqian ;
Wang, Yangdong .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2018, 57 (20) :6815-6820
[65]   Synthesis and catalytic cracking performance of Fe/Ti-ZSM-5 zeolite from attapulgite mineral [J].
Zhou, Xiaozhao ;
Liu, Yan ;
Meng, Xiangju ;
Shen, Baojian ;
Xiao, Feng-Shou .
CHINESE JOURNAL OF CATALYSIS, 2013, 34 (08) :1504-1512
[66]   Controllably tailoring external surface sites of nanosheet HZSM-5 for maximizing light olefins in catalytic cracking of n-decane [J].
Zhu, Tiantian ;
Liang, Hairui ;
Zhang, Bofeng ;
Tian, Yajie ;
Liu, Guozhu .
CHINESE JOURNAL OF CHEMICAL ENGINEERING, 2021, 38 :276-285
[67]   Residue Catalytic Cracking Process for Maximum Ethylene and Propylene Production [J].
Zhu, Xiaolin ;
Jiang, Shuai ;
Li, Chunyi ;
Chen, Xiaobo ;
Yang, Chaohe .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2013, 52 (40) :14366-14375