Kerkhoff Jana, Opitz Niklas, Peters Luca, Borrmann Dominik, Sadowski Gabriele
Department of Chemical and Biochemical Engineering, Laboratory of Thermodynamics TU Dortmund University, Emil-Figge-Str. 70, Dortmund D-44227, Germany.
INVITE GmbH, Drug Delivery and Innovation Center (DDIC), Leverkusen 51368, Germany.
Mol Pharm. 2025 Jul 7;22(7):3771-3781. doi: 10.1021/acs.molpharmaceut.5c00033. Epub 2025 Apr 16.
Drying amorphous solid dispersions (ASDs) often requires a secondary drying step, as after the first drying step, residual solvent usually remains in the ASD. Enhancing the secondary drying step of ASDs is a critical task, as it is essential to ensure that the residual solvent content meets regulatory limits. The challenge lies in the slow drying of the glassy ASD at very low solvent contents. This study performs a water-assisted drying approach that (1) accelerates residual solvent removal and (2) reduces the solvent content in the final ASD. The proposed approach involves maintaining a constant relative humidity (RH) during ASD drying, in contrast to conventional drying, which applies dry air or vacuum. We employed dynamic vapor sorption with integrated Raman spectroscopy as an analytic method to measure the water-assisted secondary-drying kinetics of ASDs at low residual solvent contents. An ASD of indomethacin and poly vinylpyrrolidone--vinyl acetate (PVPVA) containing residual amounts of ethanol was dried at 30 °C using both water-assisted and conventional drying approaches. Compared to the conventional drying, where 3.5 wt % ethanol remained in the ASD even after 1500 min, water-assisted drying at RH = 0.8 could completely remove the ethanol from the ASD in the same time frame. Modeling the ASD solution in advance using PC-SAFT (perturbed-chain statistical associating fluid theory) enabled the selection of starting compositions, preventing water-induced phase separation during the drying process. Moreover, applying the nonequilibrium (NE) version, NE-PC-SAFT, we accurately predicted the composition of the ASD solution during drying. Furthermore, we were able to predict the RH at which the residual ethanol content could be entirely removed from the ASD in a given time frame.
干燥无定形固体分散体(ASD)通常需要二次干燥步骤,因为在第一次干燥步骤之后,ASD中通常会残留溶剂。加强ASD的二次干燥步骤是一项关键任务,因为确保残留溶剂含量符合监管限制至关重要。挑战在于玻璃态ASD在极低溶剂含量下干燥缓慢。本研究采用了一种水辅助干燥方法,该方法(1)加速残留溶剂的去除,(2)降低最终ASD中的溶剂含量。与采用干燥空气或真空的传统干燥方法不同,所提出的方法涉及在ASD干燥过程中保持恒定的相对湿度(RH)。我们采用集成拉曼光谱的动态蒸汽吸附作为分析方法,来测量低残留溶剂含量下ASD的水辅助二次干燥动力学。将含有残留乙醇量的吲哚美辛与聚乙烯吡咯烷酮 - 醋酸乙烯酯(PVPVA)的ASD在30°C下分别采用水辅助干燥和传统干燥方法进行干燥。与传统干燥相比,即使经过1500分钟,ASD中仍残留3.5 wt%的乙醇,而在RH = 0.8的水辅助干燥条件下,能在相同时间内完全去除ASD中的乙醇。预先使用PC - SAFT(扰动链统计缔合流体理论)对ASD溶液进行建模,能够选择起始组成,防止干燥过程中因水引起的相分离。此外,应用非平衡(NE)版本的NE - PC - SAFT,我们准确预测了干燥过程中ASD溶液的组成。此外,我们还能够预测在给定时间内可以将ASD中残留乙醇含量完全去除时的RH。