Strategy for Scaling-up of a Microsieve Dispersion Reactor

被引:50
作者
Wang, Kai [1 ]
Lu, Yangcheng [1 ]
Luo, Guangsheng [1 ]
机构
[1] Tsinghua Univ, State Key Lab Chem Engn, Dept Chem Engn, Beijing 100084, Peoples R China
基金
中国国家自然科学基金;
关键词
Caprolactam; Microreactor; Microsieve dispersion; Minireactor; Scaling-up; NUMBERING-UP; MICROREACTOR; PARTICLES; MICROFLUIDICS; SELECTIVITY; CHEMISTRY; EFFICIENT; HYDROGEN; DEVICES; DESIGN;
D O I
10.1002/ceat.201400296
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
For the application of microreactors in industrial processes, more scaling-up strategies are still required except of the original concept, the numbering-up. A more maneuverable and economic approach, combining both similarity-up and numbering-up, is introduced as an example for an innovative strategy. CFD simulation is also applied to assist analysis and optimization of fluid distribution. Based on this concept, named similarity-up + numbering-up + simulation, a pilot-plant microsieve dispersion minireactor used to proceed the reaction of cyclohexanecarboxylic acid and oleum is designed and tested experimentally. With the contribution of similarity-up, the treating capacity of the core unit is significantly increased. Ten parallel units are integrated to form a correspondingly enhanced capacity of the microreactor which exhibits low pressure drop, stable operating performance, and excellent main product selectivity.
引用
收藏
页码:2116 / 2122
页数:7
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