Comito Marziale, Monguzzi Riccardo, Tagliapietra Silvia, Maspero Angelo, Palmisano Giovanni, Cravotto Giancarlo
Dipartimento di Scienza e Tecnologia del Farmaco, University of Turin, Via Pietro Giuria 9, 10125 Turin, Italy.
Research and Development, ACS Dobfar SpA, Via Paullo 9, 20067 Tribiano, Italy.
Pharmaceutics. 2023 Apr 23;15(5):1322. doi: 10.3390/pharmaceutics15051322.
Meropenem is currently the most common carbapenem in clinical applications. Industrially, the final synthetic step is characterized by a heterogeneous catalytic hydrogenation in batch mode with hydrogen and Pd/C. The required high-quality standard is very difficult to meet and specific conditions are required to remove both protecting groups [i.e., -nitrobenzyl (pNB) and -nitrobenzyloxycarbonyl (pNZ)] simultaneously. The three-phase gas-liquid-solid system makes this step difficult and unsafe. The introduction of new technologies for small-molecule synthesis in recent years has opened up new landscapes in process chemistry. In this context, we have investigated meropenem hydrogenolysis using microwave (MW)-assisted flow chemistry for use as a new technology with industrial prospects. The reaction parameters (catalyst amount, T, P, residence time, flow rate) in the move from the batch process to semi-continuous flow were investigated under mild conditions to determine their influence on the reaction rate. The optimization of the residence time (840 s) and the number of cycles (4) allowed us to develop a novel protocol that halves the reaction time compared to batch production (14 min vs. 30 min) while maintaining the same product quality. The increase in productivity using this semi-continuous flow technique compensates for the slightly lower yield (70% vs. 74%) obtained in batch mode.
美罗培南是目前临床应用中最常见的碳青霉烯类药物。在工业上,最终的合成步骤以氢气和钯碳在间歇模式下进行多相催化加氢为特征。所需的高质量标准很难达到,并且需要特定条件才能同时去除两个保护基团[即对硝基苄基(pNB)和对硝基苄氧羰基(pNZ)]。三相气液固体系使得这一步骤既困难又不安全。近年来,小分子合成新技术的引入为过程化学开辟了新的前景。在此背景下,我们研究了使用微波(MW)辅助流动化学进行美罗培南氢解反应,将其作为一种具有工业应用前景的新技术。在温和条件下研究了从间歇过程转变为半连续流动过程中的反应参数(催化剂量、温度、压力、停留时间、流速),以确定它们对反应速率的影响。通过优化停留时间(840秒)和循环次数(4次),我们开发了一种新方法,与间歇生产相比,反应时间减半(14分钟对30分钟),同时保持相同的产品质量。使用这种半连续流动技术提高的生产率弥补了间歇模式下略低的产率(70%对74%)。