Cyclohexanone ammoximation over TS-1 catalyst without organic solvent in a microreaction system

被引:37
作者
Hu, Yunpeng [1 ]
Dong, Chen [1 ]
Wang, Tao [1 ]
Luo, Guangsheng [1 ]
机构
[1] Tsinghua Univ, Dept Chem Engn, State Key Lab Chem Engn, Beijing 100084, Peoples R China
基金
中国国家自然科学基金;
关键词
Liquid-liquid-solid heterogeneous reaction; Cyclohexanone ammoximation; TS-1; Microreactor; TITANIUM SILICALITE-1 COMPOSITE; LIQUID-LIQUID-EXTRACTION; MASS-TRANSFER; REACTION-KINETICS; PERFORMANCE; MICROCHANNELS; MECHANISM;
D O I
10.1016/j.ces.2018.04.044
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
We herein propose a highly efficient technology for the synthesis of cyclohexanone oxime, a key intermediate for the production of caprolactam. The classical cyclohexanone ammoximation over TS-1 catalyst needs t-butanol as the organic solvent to change the reaction system from liquid-liquid-solid to liquid-solid for much better reaction performances, which greatly increases the reactor size and the downstream separation cost. In this work, a solvent-free liquid-liquid-solid heterogeneous reaction was successfully implemented in a microreaction system containing two T-junction microreactors. The effects of temperature, pressure, residence time, concentrations of reactants and catalyst on the reaction performance were systematically investigated. This developed technology resulted in a 99.87% conversion of cyclohexanone and nearly 100% selectivity to cyclohexanone oxime within 3 min. These results indicate that the new process could provide a more environmental friendly and economic approach to caprolactam industry. (C) 2018 Elsevier Ltd. All rights reserved.
引用
收藏
页码:60 / 66
页数:7
相关论文
共 33 条
[1]   Analysis and improvement of strong exothermic nitrations in microreactors [J].
Antes, J ;
Boskovic, D ;
Krause, H ;
Loebbecke, S ;
Lutz, N ;
Tuercke, T ;
Schweikert, W .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2003, 81 (A7) :760-765
[2]   ε-caprolactam:: New by-product free synthesis routes [J].
Dahlhoff, G ;
Niederer, JPM ;
Hoelderich, WF .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 2001, 43 (04) :381-441
[3]   TS-1, catalytic mechanism in cyclohexanone oxime production [J].
Dal Pozzo, L ;
Fornasari, G ;
Monti, T .
CATALYSIS COMMUNICATIONS, 2002, 3 (08) :369-375
[4]   Reaction kinetics of cyclohexanone ammoximation over TS-1 catalyst in a microreactor [J].
Dong, C. ;
Wang, K. ;
Zhang, J. S. ;
Luo, G. S. .
CHEMICAL ENGINEERING SCIENCE, 2015, 126 :633-640
[5]   Heterogeneous catalytic synthesis using microreactor technology [J].
Frost, Christopher G. ;
Mutton, Lynsey .
GREEN CHEMISTRY, 2010, 12 (10) :1687-1703
[6]   The Effect of Nanoparticles on the Mass Transfer in Liquid-Liquid Extraction [J].
Ghanadi, Asghar Mirzazadeh ;
Nasab, Amir Heydari ;
Bastani, Dariush ;
Kordi, Ali Akbar Seife .
CHEMICAL ENGINEERING COMMUNICATIONS, 2015, 202 (05) :600-605
[7]  
[顾耀明 GU Yaoming], 2010, [化工进展, Chemical Industry and Engineering Progress], V29, P187
[8]   A micromixer with two-layer serpentine crossing channels having excellent mixing performance at low Reynolds numbers [J].
Hossain, Shakhawat ;
Lee, Insu ;
Kim, Sun Min ;
Kim, Kwang-Yong .
CHEMICAL ENGINEERING JOURNAL, 2017, 327 :268-277
[9]   Heterogeneous Catalytic Hydrogenation Reactions in Continuous-Flow Reactors [J].
Irfan, Muhammad ;
Glasnov, Toma N. ;
Kappe, C. Oliver .
CHEMSUSCHEM, 2011, 4 (03) :300-316
[10]   Kinetics of liquid-phase cyclohexanone ammoximation over a titanium silicate [J].
Kulkova, NV ;
Kotova, VG ;
Kvyathovskaya, MY ;
Murzin, DY .
CHEMICAL ENGINEERING & TECHNOLOGY, 1997, 20 (01) :43-46