Davidson School of Chemical Engineering, Purdue University, West Lafayette, IN 47907, USA; Dr. Reddy's Laboratories Ltd., IPDO, Bachupally, Hyderabad 500090, India.
Dr. Reddy's Laboratories Ltd., IPDO, Bachupally, Hyderabad 500090, India.
Int J Pharm. 2022 Nov 5;627:122172. doi: 10.1016/j.ijpharm.2022.122172. Epub 2022 Sep 7.
In this paper, continuous crystallization of Atorvastatin calcium (ASC) using a continuous oscillatory baffled crystallizer (COBC) has been investigated. Like most API manufacturing, ASC is manufactured batchwise and the pure API is recovered via batch combined cooling and antisolvent crystallization (CCAC) process, which has the challenges of low productivity, wide crystal size distribution (CSD) and sometimes polymorphic form contamination. To overcome the limitations of the batch crystallization, continuous crystallization of ASC was studied in a NiTech (United Kingdom) DN15 COBC, manufactured by Alconbury Weston Ltd. (AWL, United Kingdom), with the aim to improve productivity and CSD of the desired polymorph. The COBC has the advantage of high heat transfer rates and improved mixing that significantly reduces the crystallization time. It also has the advantage of spatial temperature distribution and multiple addition ports to control supersaturation and hence the crystallization process. This work uses an array of process analytical technology (PAT) tools to assess key process parameters that affect the polymorphic outcome and CSD. Two parameters were found to have significant impact on the polymorph, they are ratio of solvent to antisolvent at the point of mixing of the two streams and presence of seeds. The splitting of antisolvent into two addition ports in the COBC was found to give the desired form. The CCAC of ASC in COBC was found to be -30-fold more productive than the batch CCAC process. The cycle time for generating 100 g of desired polymorphic form of ASC also significantly reduced from 22 h in batch process to 12 min in the COBC. The crystals obtained using a CCAC process in a COBC had a narrower CSD compared to that from a batch crystallization process.
本文研究了阿托伐他汀钙(ASC)在连续振荡挡板结晶器(COBC)中的连续结晶。与大多数原料药制造一样,ASC 采用分批式生产,通过分批冷却和反溶剂结晶(CCAC)工艺回收纯原料药,该工艺存在生产效率低、晶体粒度分布(CSD)宽且有时多晶型污染的挑战。为了克服分批结晶的局限性,研究了 ASC 在 NiTech(英国)DN15 COBC 中的连续结晶,该 COBC 由 Alconbury Weston Ltd.(AWL,英国)制造,目的是提高所需多晶型的生产效率和 CSD。COBC 具有传热速率高和混合效果好的优点,可显著缩短结晶时间。它还具有空间温度分布和多个添加口的优点,可控制过饱和度,从而控制结晶过程。这项工作使用一系列过程分析技术(PAT)工具来评估影响多晶型结果和 CSD 的关键工艺参数。发现有两个参数对多晶型有显著影响,它们是两种流混合点处溶剂与反溶剂的比例和晶种的存在。在 COBC 中将反溶剂分成两个添加口被发现可以得到所需的形式。在 COBC 中,ASC 的 CCAC 比批处理 CCAC 过程的生产效率高 30 倍。生成 100g 所需 ASC 多晶型的循环时间也从批处理过程中的 22 小时显著缩短到 COBC 中的 12 分钟。与批处理结晶过程相比,使用 COBC 中的 CCAC 工艺获得的晶体具有更窄的 CSD。