纳滤
对映选择合成
过程开发
外消旋化
工艺工程
渗透
桥接(联网)
对映体
工艺设计
过程(计算)
化学
分离过程
膜
选择性
计算机科学
生化工程
有机化学
色谱法
过程集成
工程类
催化作用
计算机网络
生物化学
操作系统
作者
Aron K. Beke,György Székely
标识
DOI:10.1016/j.memsci.2022.121020
摘要
Organic solvent nanofiltration (OSN) is a low-energy alternative for continuous separations in the chemical industry. As the pharmaceutical sector increasingly turns toward continuous manufacturing, OSN could become a sustainable solution for chiral separations. Here we present the first comprehensive theoretical assessment of enantioselective OSN processes. Lumped dynamic models were developed for various system configurations, including structurally diverse nanofiltration cascades and single-stage separations with side-stream recycling and in situ racemization. Enantiomer excess and recovery characteristics of the different processes were assessed in terms of the solute rejection values of the enantiomer pairs. The general feasibility of stereochemical resolution using OSN processes is discussed in detail. Fundamental connections between rejection selectivity, permeance selectivity, and enantiomer excess limitations are revealed. Quantitative process performance examples are presented based on theoretical rejection scenarios and cases from the literature on chiral membranes. A model-based prediction tool can be found on www.osndatabase.com to aid researchers in connecting materials development results with early-stage process performance assessments.
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