聚乙二醇
化学计量学
化学
亚硫酸盐
连续搅拌釜式反应器
过程(计算)
化学工程
材料科学
有机化学
物理化学
计算机科学
工程类
操作系统
作者
Jichang Wei,Yinli Liu,Yuchen Sun,Jun Bai,He Gao,Zhaojun Yang,Long Pan
标识
DOI:10.1002/chem.202304319
摘要
Abstract Many macrocyclic compounds are attractive drug‐like molecules or intermediates due to their special properties. However, the bulk synthesis of such compounds are hindered by the necessity of using diluted solutions, in order to prevent intermolecular reactions that yields oligomer impurities, thereby resulting in a low production efficiency. Such challenge can be adequately addressed by using continuous reactors, allowing improved efficiency with smaller space footprints. In this work, we proposed a novel continuous process for the synthesis of a macrocyclic sulfite of tetraethylene glycol (PEG4‐MCSi), which is a precursor to a very useful building block, PEG4‐macrocyclic sulfate (PEG4‐MCS). The basic reaction parameters, including stoichiometry and temperature, were first confirmed with small batch reactions, and the effectiveness of coiled reactors and continuous stirred tank reactors (CSTRs) were compared. Cascaded CSTRs were proven to be suitable, and the reaction parameters were subject to further optimization to give a robust continuous process. The process was then tested with 4 parallel runs for up to 64 h. Finally, the merits and demerits of batch and continuous reactions were also compared, demonstrating the suitability of latter in the bulk production of macrocyclic PEG‐MCSi compounds.
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