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
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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