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Understanding and optimization of the secondary drying step of a freeze-drying process: a case study

机译:冷冻干燥过程二次干燥步骤的理解与优化:案例研究

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The objective of this study was to build an understanding and optimize the secondary drying step of a freeze-drying process using a drug formulation from Fresenius Kabi (FK1) as a case study. For this purpose, a design of experiments (DoE) was developed to study the influence of drying temperature, drying time, vial position, and chamber pressure on moisture content and glass transition temperature of FK1. The results obtained herein showed that the influence of drying temperature on moisture content and glass transition temperature was strong at short drying time, implying that increasing drying temperature could lead to a significant decrease in the required drying time to achieve a designed moisture content and glass transition temperature. Variation in chamber pressure from 0.05-0.40 mbar showed insignificant influence on moisture content and glass transition temperature. Small variations in moisture content and glass transition temperature with respect to vial position were also observed, where edge vials had higher moisture content and, consequently, lower glass transition temperature than center vials. Further, the results from the DoE were utilized to construct a process design space (PDS) for the secondary drying step of FK1. Experimental verification of the PDS demonstrated an excellent agreement between the PDS-defined and experimentally-determined moisture content and glass transition temperature values. Thus, the PDS facilitated process optimization of FK1 and could serve as an important tool during scale-up and transfer of the process.
机译:本研究的目的是以弗雷森尤斯·卡比(FK1)的药物制剂为例,了解并优化冷冻干燥过程中的二次干燥步骤。为此,开发了一种实验设计(DoE),以研究干燥温度、干燥时间、小瓶位置和小室压力对FK1的水分含量和玻璃化转变温度的影响。本文获得的结果表明,在较短的干燥时间内,干燥温度对水分含量和玻璃化转变温度的影响很大,这意味着提高干燥温度可以显著缩短所需的干燥时间,以达到设计的水分含量和玻璃化转变温度。在0.05-0.40毫巴之间的腔室压力变化对水分含量和玻璃化转变温度的影响不显著。还观察到水分含量和玻璃化转变温度随小瓶位置的微小变化,其中边缘小瓶的水分含量较高,因此玻璃化转变温度低于中心小瓶。此外,利用能源部的结果为FK1的二次干燥步骤构建工艺设计空间(PDS)。PDS的实验验证表明,定义的PDS与实验确定的水分含量和玻璃化转变温度值非常一致。因此,PDS促进了FK1的工艺优化,可以作为工艺放大和转移过程中的重要工具。

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