Investigations Concerning the Residence Time Distribution of Twin-Screw-Extrusion Processes as Indicator for Inherent Mixing

被引:17
作者
Wesholowski, Jens [1 ]
Berghaus, Andreas [2 ]
Thommes, Markus [1 ]
机构
[1] TU Dortmund Univ, Inst Solids Proc Engn, D-44227 Dortmund, Germany
[2] COLVISTEC AG, D-12489 Berlin, Germany
来源
PHARMACEUTICS | 2018年 / 10卷 / 04期
基金
欧盟地平线“2020”;
关键词
modeling; process control; residence time; twin-dispersion-model; twin-screw-extrusion; HOT-MELT EXTRUSION; DISPERSION;
D O I
10.3390/pharmaceutics10040207
中图分类号
R9 [药学];
学科分类号
1007 ;
摘要
Over recent years Twin-Screw-Extrusion (TSE) has been established as a platform technology for pharmaceutical manufacturing. Compared to other continuous operation, one of the major benefits of this method is the combination of several unit operations within one apparatus. Several of these are linked to the Residence Time Distribution (RTD), which is typically expressed by the residence time density function. One relevant aspect for pharmaceutical processes is the mixing capacity, which is represented by the width of this distribution. In the frame of this study the influence of the mass flow, the temperature and the screw-barrel clearance were investigated for a constant barrel load (specific feed load, SFL). While the total mass flow as well as the external screw diameter affected the mixing performance, the barrel temperature had no influence for the investigated range. The determined results were additionally evaluated with respect to a fit to the Twin-Dispersion-Model (TDM). This model is based on the superimposition of two mixing functions. The correlations between varied process parameters and the obtained characteristic model parameters proved this general physical view on extrusion.
引用
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页数:10
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