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颗粒分层:使用不同种类的加工设备放大的考虑因素。

Pellet layering: scale-up considerations using different kinds of processing equipment.

机构信息

Boehringer Ingelheim Pharma GmbH & Co. KG, Ingelheim, Germany.

出版信息

Drug Dev Ind Pharm. 2012 Dec;38(12):1494-503. doi: 10.3109/03639045.2011.653815. Epub 2012 Mar 28.

Abstract

OBJECTIVE

In this study an aqueous suspension of poorly water-soluble HCT (hydrochlorothiazide) was layered on small spherical starter cores with a drug content in the final pellets of 30%. The aim was to compare different kinds of processing equipment (Wurster fluid-bed, CPS rotor fluid-bed and drum coater) in view of process efficiency, process duration and feasibility to scale-up.

RESULTS

In a pilot scale drum coater, it was possible to achieve the desired LE (layering efficiency) and yield specifications (both >95%), but the process duration was at least 202 min. In the small scale Wurster fluid-bed machine, it was possible to reduce the process time for an optimized process from 67 min to 41 min. However, the acceleration of the process led to an increase of agglomerates and the same process took at least 114 min in the scale-up experiments. A small scale CPS rotor processor with a cone-shaped disc was superior to the conventional planar rotor disc design, regarding yield and agglomerates. This rotor process was both, fast and highly efficient (yield: 98.4%; LE: 99.3%). The high quality of the process was also observed for the pilot scale batches, in which neither considerable losses of drug (LE ≥ 98.6%) nor formation of agglomerates occurred. The absolute spray rate in this pilot scale process was 85 kg/h.

CONCLUSION

Best results were achieved with the CPS rotor technology. With a duration of 29 min (small scale) and 44 min (pilot scale) it was the fastest option to produce layered pellets.

摘要

目的

在本研究中,将难溶于水的 HCT(氢氯噻嗪)的水性混悬液涂覆在小的球形起始核上,最终颗粒中的药物含量为 30%。目的是比较不同类型的加工设备(Wurster 流化床、CPS 转子流化床和转鼓包衣机)在效率、过程持续时间和放大可行性方面的差异。

结果

在中试规模的转鼓包衣机中,有可能实现所需的包衣效率(LE)和收率规格(均>95%),但过程持续时间至少为 202 分钟。在小型 Wurster 流化床机中,可以将优化过程的工艺时间从 67 分钟减少到 41 分钟。然而,工艺的加速导致团聚体的增加,在放大实验中相同的工艺需要至少 114 分钟。带有锥形盘的小型 CPS 转子处理器在产率和团聚体方面优于传统的平面转子盘设计。该转子工艺既快速又高效(产率:98.4%;LE:99.3%)。在中试规模批次中也观察到了工艺的高质量,药物损失不大(LE≥98.6%),也没有形成团聚体。在该中试规模工艺中,绝对喷雾速率为 85kg/h。

结论

CPS 转子技术的结果最佳。其在小试规模(29 分钟)和中试规模(44 分钟)的持续时间内是生产包衣颗粒最快的选择。

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