微型反应器
产量(工程)
动能
动力学
化学
过程(计算)
工艺工程
间歇式反应器
化学工程
热力学
有机化学
计算机科学
催化作用
程序设计语言
工程类
物理
量子力学
作者
Ting Wang,Junnan Wang,Chengxiang He,Zhongdong Wang,Yating Li,Chunying Zhu,Youguang Ma,Taotao Fu
出处
期刊:Reaction Chemistry and Engineering
[The Royal Society of Chemistry]
日期:2024-01-01
卷期号:9 (7): 1947-1958
被引量:1
摘要
After optimizing the continuous synthesis process of DTD, the yield can reach 92.22%, which is higher than the yield in the batch reactor. Meanwhile, the reaction kinetics model in the microreactor is also established.
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