工作流程
吞吐量
计算机科学
催化作用
工艺工程
高通量筛选
产量(工程)
自动化
化学
纳米技术
生化工程
组合化学
材料科学
热力学
工程类
有机化学
物理
数据库
电信
机械工程
生物化学
无线
标识
DOI:10.1021/acs.oprd.1c00213
摘要
High-throughput experimentation (HTE) has become integral to the pharmaceutical industry with most major pharmaceutical companies investing in automation and high-throughput screening technologies. Testing hundreds of reactions in parallel has distinct advantages; however, one clear disadvantage is that performing a reaction on micromolar scale is not always indicative of the reaction's performance on multikilogram scale. Additionally, a great deal of information is lost by looking at a single time point. Valuable data around intermediates, over-reaction, catalyst induction periods, and so forth are invisible to a typical HTE workflow, which involves analyzing reactions at a single time point (e.g., 18 h). We envisioned a workflow in which time courses for each well of a high-throughput screen were collected. With this change in strategy, it could then become possible to complete high-throughput screening, select reaction conditions, gather kinetic information, and successfully build a kinetic model in less than 1 week. A kinetic model consisting of scale-independent parameters allows for virtual reaction optimization where the input concentrations, catalyst loading, and temperature can all be simulated and adjusted to understand their impact on yield or quality in a matter of seconds. A case study is presented with a transition metal salt/TMSCl-catalyzed aza-Michael reaction to showcase the performance and robustness of the high-throughput kinetic platform. A reaction progress kinetic analysis approach is utilized to quickly screen the rates of 48 catalyst/solvent combinations and create a mechanistic model. The first-principles kinetic model provides support for a proposed mechanism of dual activation by TMSCl.
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