Research Center Pharmaceutical Engineering, Inffeldgasse 13, 8010 Graz, Austria.
Worldwide Research and Development, Pfizer Inc., Groton, CT, USA.
Int J Pharm. 2021 Oct 25;608:121065. doi: 10.1016/j.ijpharm.2021.121065. Epub 2021 Sep 2.
Continuous powder mixing is an important technology used in the development and manufacturing of solid oral dosage forms. Since critical quality attributes of the final product greatly depend on the performance of the mixing step, an analysis of such a process using the Discrete Element Method (DEM) is of crucial importance. On one hand, the number of expensive experimental runs can be reduced dramatically. On the other hand, numerical simulations can provide information that is very difficult to obtain experimentally. In order to apply such a simulation technology in product development and to replace experimental runs, an intensive model validation step is required. This paper presents a DEM model of the vertical continuous mixing device termed CMT (continuous mixing technology) and an extensive validation workflow. First, a cohesive contact model was calibrated in two small-scale characterization experiments: a compression test with spring-back and a shear cell test. An improved, quicker calibration procedure utilizing the previously calibrated contact models is presented. The calibration procedure is able to differentiate between the blend properties caused by different API particle sizes in the same formulation. Second, DEM simulations of the CMT were carried out to determine the residence time distribution (RTD) of the material inside the mixer. After that, the predicted RTDs were compared with the results of tracer spike experiments conducted with two blend material properties at two mass throughputs of 15 kg/h and 30 kg/h. Additionally, three hold-up masses (500, 730 and 850 g) and three impeller speeds (400, 440 and 650 rpms) were considered. Finally, both RTD datasets from DEM and tracer experiments were used to predict the damping behavior of incoming feeder fluctuations and the funnel of maximum duration and magnitude of incoming deviations that do not require a control action. The results for both tools in terms of enabling a control strategy (the fluctuation damping and the funnel plot) are in excellent agreement, indicating that DEM simulations are well suited to replace process-scale tracer spike experiments to determine the RTD.
连续粉末混合是开发和制造固体口服剂型的重要技术。由于最终产品的关键质量属性在很大程度上取决于混合步骤的性能,因此使用离散元法 (DEM) 对这样的过程进行分析至关重要。一方面,可以大大减少昂贵的实验运行次数。另一方面,数值模拟可以提供非常难以通过实验获得的信息。为了在产品开发中应用这种模拟技术并替代实验运行,需要进行密集的模型验证步骤。本文提出了一种称为 CMT(连续混合技术)的垂直连续混合设备的 DEM 模型和广泛的验证工作流程。首先,在两个小规模的特征化实验中校准了粘性接触模型:带有回弹的压缩测试和剪切池测试。提出了一种利用先前校准的接触模型的改进、更快的校准程序。该校准程序能够区分同一配方中不同 API 粒径引起的混合物特性。其次,对 CMT 进行了 DEM 模拟,以确定物料在混合器内的停留时间分布 (RTD)。之后,将预测的 RTD 与使用两种混合物特性在两个质量吞吐量(15kg/h 和 30kg/h)进行示踪剂脉冲实验的结果进行了比较。此外,还考虑了三个持液量(500、730 和 850g)和三个叶轮转速(400、440 和 650rpm)。最后,使用 DEM 和示踪实验的 RTD 数据集来预测进料波动的阻尼行为和进料最大持续时间和幅度的漏斗,而无需控制动作。两种工具在启用控制策略(波动阻尼和漏斗图)方面的结果非常吻合,表明 DEM 模拟非常适合替代过程规模的示踪剂脉冲实验来确定 RTD。