Operations Science and Technology, AbbVie, Illinois, North Chicago, 60064, USA.
Center for Chemical Sensors Development/Chemical Imaging Center, University of Puerto Rico, Mayaguez, Puerto Rico, 00680, USA.
AAPS PharmSciTech. 2021 Oct 14;22(7):249. doi: 10.1208/s12249-021-02148-x.
Using discrete element method (DEM) modeling and near-infrared (NIR) spectroscopy, the feasibility of powder mixing in the initial pre-melting zones of a twin screw extruder using two independent feeders was studied. Previous work in the pharmaceutical and food industry has focused on mixing when materials are melted or on material homogeneity at the extruder's output. Depending on the formulation, ensuring a fully blended formulation prior to melting may be desired. Experiments were conducted using a Coperion ZSK-18 extruder to evaluate if blend uniformity can be achieved by exploring screw configuration, screw speed, and powder feed rate. As powder exited the extruder and deposited on a conveyor belt, an in-line NIR spectrophotometer measured spectra of material. Chemometric-based models predicted unknown concentrations to evaluate if blend uniformity was achieved. Using the EDEM software, Hertz-Mindlin contact model, and dimensions of the extruder, DEM simulations complemented the experimental work. The DEM computational models provided understanding of mixing patterns inside the extruder at particle scale and helped select the screw configuration before doing experimentation. The simulations showed good axial mixing for all the screw configurations studied, while good cross (radial) mixing was only observed for the screw configuration with 90-degree kneading elements. Therefore, the screw configuration with two 90-degree kneading elements was chosen for the experimental study. The RTD profiles when using a screw configuration with only conveying screw elements are comparable to a plug flow reactor (PFR), while the profiles when using kneading elements are more comparable to an ideal continuous stirred tank reactor (CSTR). For the screw configuration with 90 degrees kneading elements, the mean residence time (MRT) decreases with an increase in the screw speed. Experimental NIR spectra showed that concentrations can be predicted with an error of 2%. It was demonstrated that the twin screw extruder can provide proper dry powder mixing of two powder feed streams based on a unit dose scale, enabling continuous powder mixing prior to the melting zone in the extruder for the formulation studied with a cohesive API. This setup may also work for other types of formulations. These studies can help in developing lean hot melt as well as wet extrusion/granulation processes using twin screw extruders for the continuous manufacturing of oral solid dosage products.
利用离散元法(DEM)建模和近红外(NIR)光谱技术,研究了在双螺杆挤出机的初始预熔融区使用两个独立进料器进行粉末混合的可行性。制药和食品行业的先前研究集中在材料熔融时的混合或在挤出机输出处的材料均一性上。根据配方的不同,在熔融之前确保完全混合的配方可能是需要的。实验在 Coperion ZSK-18 挤出机上进行,以评估通过探索螺杆构型、螺杆速度和粉末进料速率是否可以实现混合均匀性。当粉末从挤出机中出来并沉积在输送带上时,在线 NIR 分光光度计测量材料的光谱。基于化学计量学的模型预测未知浓度以评估是否实现了混合均匀性。使用 EDEM 软件、赫兹-明克林接触模型和挤出机的尺寸,DEM 模拟补充了实验工作。DEM 计算模型提供了在颗粒尺度上对挤出机内部混合模式的理解,并在进行实验之前帮助选择螺杆构型。模拟结果表明,所有研究的螺杆构型均具有良好的轴向混合性,而只有具有 90 度捏合元件的螺杆构型才观察到良好的横向(径向)混合性。因此,选择了具有两个 90 度捏合元件的螺杆构型进行实验研究。仅使用输送螺杆元件的螺杆构型的 RTD 曲线与塞流反应器(PFR)相当,而使用捏合元件的曲线则更类似于理想的连续搅拌釜式反应器(CSTR)。对于具有 90 度捏合元件的螺杆构型,随着螺杆速度的增加,平均停留时间(MRT)减小。实验 NIR 光谱表明,可以以 2%的误差预测浓度。结果表明,双螺杆挤出机可以在基于单位剂量规模的情况下对两种粉末进料流进行适当的干粉混合,从而为在挤出机的熔融区之前为所研究的具有粘性 API 的配方提供连续粉末混合。这种设置也可能适用于其他类型的配方。这些研究有助于在使用双螺杆挤出机连续制造口服固体制剂时开发用于 lean hot melt 以及湿挤压/造粒工艺。