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考虑颗粒大小的药物颗粒半连续流化床干燥建模。

Modeling of Semicontinuous Fluid Bed Drying of Pharmaceutical Granules With Respect to Granule Size.

机构信息

Department of Data Analysis and Mathematical Modelling, BIOMATH, Ghent University, Oost-Vlaanderen, Belgium; Laboratory of Pharmaceutical Process Analytical Technology, Department of Pharmaceutical Analysis, Ghent University, Oost-Vlaanderen, Belgium.

Discovery, Product Development and Supply, Janssen, Pharmaceutical Companies of Johnson & Johnson, Beerse, Belgium.

出版信息

J Pharm Sci. 2019 Jun;108(6):2094-2101. doi: 10.1016/j.xphs.2019.01.013. Epub 2019 Jan 19.

Abstract

In the transition of the pharmaceutical industry from batchwise to continuous drug product manufacturing, the drying process has proven challenging to control and understand. In a semicontinuous fluid bed dryer, part of the ConsiGma™ wet granulation line, the aforementioned production methods converge. Previous research has shown that the evolution of moisture content of the material in this system shows strong variation in function of the granule size, making the accurate prediction of this pharmaceutical critical quality attribute a complex case. In this work, the evolution of moisture content of the material in the system is modeled by a bottom-up approach. A single granule drying kinetics model is used to predict the moisture content evolution of a batch of material of a heterogeneous particle size, where it is the first time that the single granule drying mechanism is validated for different granule sizes. The batch approach was validated when the continuous material inflow rate and filling time of the dryer cell are constant. The original single granule drying kinetics model has been extended to capture the granules' equilibrium moisture content. Finally, the influence of drying air temperature is captured well with a droplet energy balance for the granules.

摘要

在制药行业从分批式向连续式药物产品制造的转变中,干燥过程已被证明难以控制和理解。在部分 ConsiGma™湿法制粒线的半连续流化床干燥器中,上述生产方法汇聚在一起。先前的研究表明,该系统中物料含水量的演变与颗粒大小呈强函数关系,这使得对这一制药关键质量属性的准确预测成为一个复杂的问题。在这项工作中,采用自下而上的方法对系统中物料的含水量演变进行建模。使用单个颗粒干燥动力学模型来预测具有不均匀粒径的一批物料的含水量演变,这是首次验证单个颗粒干燥机制适用于不同的颗粒尺寸。当干燥器单元的连续物料流入率和填充时间恒定时,对批处理方法进行了验证。原始的单个颗粒干燥动力学模型已扩展到捕获颗粒的平衡含水量。最后,通过颗粒的液滴能量平衡很好地捕捉到了干燥空气温度的影响。

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