Institute of Pharmaceutics and Biopharmaceutics, Heinrich-Heine-University Duesseldorf, Duesseldorf, Germany.
Eur J Pharm Biopharm. 2012 Jan;80(1):122-9. doi: 10.1016/j.ejpb.2011.10.002. Epub 2011 Oct 8.
The aim of this study was to use a mechanistically realistic mathematical model based on Fick's second law to quantitatively predict the release profiles from solid lipid extrudates consisting of a ternary matrix. Diprophylline was studied as a freely water-soluble model drug, glycerol tristearate as a matrix former and polyethylene glycol or crospovidone as a pore former (blend ratio: 50:45:5%w/w/w). The choice of these ratios is based on former studies. Strains with a diameter of 0.6, 1, 1.5, 2.7 and 3.5mm were prepared using a twin-screw extruder at 65 °C and cut into cylinders of varying lengths. Drug release in demineralised water was measured using the USP 32 basket apparatus. Based on SEM pictures of extrudates before and after exposure to the release medium as well as on DSC measurements and visual observations, an analytical solution of Fick's second law of diffusion was identified in order to quantify the resulting diprophylline release kinetics from the systems. Fitting the model to one set of experimentally determined diprophylline release kinetics from PEG containing extrudates allowed determining the apparent diffusion coefficient of this drug (or water) in this lipid matrix. Knowing this value, the impact of the dimensions of the cylinders on drug release could be quantitatively predicted. Importantly, these theoretical predictions could be confirmed by independent experimental results. Thus, diffusion is the dominant mass transport mechanism controlling drug release in this type of advanced drug delivery systems. In contrast, theoretical predictions of the impact of the device dimensions in the case of crospovidone containing extrudates significantly underestimated the real diprophylline release rates. This could be attributed to the disintegration of this type of dosage forms when exceeding a specific minimal device diameter. Thus, mathematical modelling can potentially significantly speed up the development of solid lipid extrudates, but care has to be taken that none of the assumptions the mathematical theory is based on is violated.
本研究旨在使用基于菲克第二定律的机械合理的数学模型,定量预测由三元基质组成的固体脂质挤出物的释放曲线。二羟丙茶碱被用作自由水溶性模型药物,甘油三硬脂酸酯作为基质形成剂,聚乙二醇或交联聚维酮作为孔形成剂(混合比:50:45:5%w/w/w)。这些比例的选择基于先前的研究。在 65°C 下使用双螺杆挤出机制备直径为 0.6、1、1.5、2.7 和 3.5mm 的应变,将其切成不同长度的圆柱体。在去矿物质水中使用 USP 32 篮法测量药物释放。基于挤出物在暴露于释放介质前后的 SEM 图片以及 DSC 测量和视觉观察,确定了菲克第二定律扩散的解析解,以量化系统中产生的二羟丙茶碱释放动力学。将模型拟合到一组含有 PEG 的挤出物的实验确定的二羟丙茶碱释放动力学中,允许确定该药物(或水)在该脂质基质中的表观扩散系数。知道这个值,就可以定量预测圆柱体尺寸对药物释放的影响。重要的是,这些理论预测可以通过独立的实验结果得到证实。因此,扩散是控制此类先进药物传递系统中药物释放的主要传质机制。相比之下,含有交联聚维酮的挤出物的装置尺寸对药物释放的影响的理论预测大大低估了实际的二羟丙茶碱释放率。这可以归因于当超过特定的最小装置直径时,这种类型的剂型的崩解。因此,数学建模有可能大大加快固体脂质挤出物的开发速度,但必须注意数学理论所基于的假设不会被违反。