Highly stable monolithic titanium silicalite-1 catalyst for 1-butene epoxidation

被引:3
|
作者
Zuo, Yi [1 ]
Zhang, Bosong [1 ]
Li, Tonghui [1 ]
Zhang, Miao [1 ]
Fan, Jialin [1 ]
Liu, Min [1 ]
Xu, Junbo [2 ]
Yang, Chao [2 ]
Yang, Hong [3 ]
Guo, Xinwen [1 ]
机构
[1] Dalian Univ Technol, PSU DUT Joint Ctr Energy Res, Sch Chem Engn, Dept Catalysis Chem & Engn,State Key Lab Fine Che, Dalian 116024, Peoples R China
[2] Chinese Acad Sci, Inst Proc Engn, Key Lab Green Proc & Engn, Beijing 100190, Peoples R China
[3] Univ Western Australia, Dept Mech Engn, Perth, WA 6009, Australia
关键词
1-butene epoxidation; heat conductivity; monolithic catalyst; reaction kinetics; TS-1; HYDROGEN-PEROXIDE; PROPYLENE EPOXIDATION; PERFORMANCE;
D O I
10.1002/aic.17870
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A monolithic titanium silicalite-1 (TS-1) catalyst was prepared by coating TS-1 onto a specially designed stainless-steel support. The catalyst was used in 1-butene epoxidation, a strong exothermic reaction, to produce butene oxide in a fixed-bed reactor. Compared with the traditional extruded TS-1, the monolithic catalyst demonstrates excellent catalytic stability and reusability. To understand the reason for this performance, heat conduction behaviors of the monolithic and extruded catalysts were studied and compared. This was accomplished by firstly developing a kinetic model to determine reaction kinetic parameters, and then simulating the temperature distribution within the reactor. It revealed a much lower temperature-rise over the monolithic catalyst than over the extruded catalyst. This study demonstrates that the stainless-steel support of the monolithic catalyst is effective in dissipating high reaction heat of 1-butene epoxidation, thus limits local temperature-rise within the reactor. This inhibits the formation of channel-blocking byproducts and improves the catalytic stability.
引用
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页数:12
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