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本文引用的文献

1
Evaluation of manometric temperature measurement, a process analytical technology tool for freeze-drying: Part I, product temperature measurement.冻干过程分析技术工具——压力温度测量的评估:第一部分,产品温度测量
AAPS PharmSciTech. 2006 Mar;7(1):E95-E103. doi: 10.1208/pt070114. Epub 2017 Mar 8.
2
Rapid determination of dry layer mass transfer resistance for various pharmaceutical formulations during primary drying using product temperature profiles.利用产品温度曲线快速测定各种药物制剂在一次干燥过程中的干层传质阻力。
Int J Pharm. 2006 Apr 26;313(1-2):99-113. doi: 10.1016/j.ijpharm.2006.01.036. Epub 2006 Feb 28.
3
Heat and mass transfer scale-up issues during freeze drying: II. Control and characterization of the degree of supercooling.冷冻干燥过程中的传热传质放大问题:II. 过冷度的控制与表征
AAPS PharmSciTech. 2004 Aug 5;5(4):e58. doi: 10.1208/pt050458.
4
Heat and mass transfer scale-up issues during freeze-drying, I: atypical radiation and the edge vial effect.冷冻干燥过程中的传热传质放大问题,I:非典型辐射与边缘瓶效应
AAPS PharmSciTech. 2003;4(2):E14. doi: 10.1208/pt040214.
5
The ice nucleation temperature determines the primary drying rate of lyophilization for samples frozen on a temperature-controlled shelf.冰核化温度决定了在控温搁板上冷冻的样品冻干的一次干燥速率。
J Pharm Sci. 2001 Jul;90(7):860-71. doi: 10.1002/jps.1039.
6
Physical chemistry of freeze-drying: measurement of sublimation rates for frozen aqueous solutions by a microbalance technique.冷冻干燥的物理化学:用微量天平技术测量冷冻水溶液的升华速率
J Pharm Sci. 1983 Jun;72(6):635-50. doi: 10.1002/jps.2600720614.
7
Use of laboratory data in freeze drying process design: heat and mass transfer coefficients and the computer simulation of freeze drying.实验室数据在冷冻干燥工艺设计中的应用:传热传质系数及冷冻干燥的计算机模拟
J Parenter Sci Technol. 1985 May-Jun;39(3):115-39.
8
Process control in freeze drying: determination of the end point of sublimation drying by an electronic moisture sensor.冷冻干燥中的过程控制:通过电子湿度传感器确定升华干燥的终点
J Parenter Sci Technol. 1989 Mar-Apr;43(2):60-6.

QbD 案例研究:冷冻干燥循环参数的贝叶斯预测。

A QbD case study: Bayesian prediction of lyophilization cycle parameters.

机构信息

Purdue University, Discovery Park, West Lafayette, Indiana, USA.

出版信息

AAPS PharmSciTech. 2011 Mar;12(1):442-8. doi: 10.1208/s12249-011-9598-x. Epub 2011 Mar 4.

DOI:10.1208/s12249-011-9598-x
PMID:21373766
原文链接:https://pmc.ncbi.nlm.nih.gov/articles/PMC3066384/
Abstract

As stipulated by ICH Q8 R2 (1), prediction of critical process parameters based on process modeling is a part of enhanced, quality by design approach to product development. In this work, we discuss a Bayesian model for the prediction of primary drying phase duration. The model is based on the premise that resistance to dry layer mass transfer is product specific, and is a function of nucleation temperature. The predicted duration of primary drying was experimentally verified on the lab scale lyophilizer. It is suggested that the model be used during scale-up activities in order to minimize trial and error and reduce costs associated with expensive large scale experiments. The proposed approach extends the work of Searles et al. (2) by adding a Bayesian treatment to primary drying modeling.

摘要

根据 ICH Q8 R2(1)的规定,基于过程建模预测关键工艺参数是产品开发增强型设计质量方法的一部分。在这项工作中,我们讨论了一种用于预测初级干燥阶段持续时间的贝叶斯模型。该模型基于以下前提:干燥层传质阻力是特定于产品的,并且是成核温度的函数。在实验室规模的冷冻干燥机上对初级干燥的预测持续时间进行了实验验证。建议在放大活动中使用该模型,以尽量减少试错并降低与昂贵的大规模实验相关的成本。所提出的方法通过向初级干燥建模中添加贝叶斯处理扩展了 Searles 等人的工作(2)。