表征(材料科学)
过程(计算)
生物反应器
比例(比率)
工艺工程
材料科学
放大
计算机科学
生化工程
纳米技术
工程类
化学
物理
操作系统
经典力学
有机化学
量子力学
作者
Vincent Bernemann,Jürgen Fitschen,Marco Leupold,Karl‐Heinz Scheibenbogen,Marc Maly,Marko Hoffmann,Thomas Wucherpfennig,Michael Schlüter
出处
期刊:Fluids
[Multidisciplinary Digital Publishing Institute]
日期:2024-05-16
卷期号:9 (5): 115-115
被引量:6
标识
DOI:10.3390/fluids9050115
摘要
The reliable transfer of bioprocesses from single-use bioreactors (SUBs) of different scales to conventional stainless steel stirred-tank bioreactors is of steadily growing interest. In this publication, a scale-up study for SUBs with volumes of 200 L and 2000 L and the transfer to an industrial-scale conventional stainless steel stirred-tank bioreactor with a volume of 15,000 L is presented. The scale-up and transfer are based on a comparison of mixing times and the modeling of volumetric mass transfer coefficients kLa, measured in all three reactors in aqueous PBS/Kolliphor solution. The mass transfer coefficients are compared with the widely used correlation of van’t Riet at constant stirrer tip speeds. It can be shown that a van’t Riet correlation enables a robust and reliable prediction of mass transfer coefficients on each scale for a wide range of stirrer tip speeds and aeration rates. The process transfer from single-use bioreactors to conventional stainless steel stirred-tank bioreactors is proven to be uncritical concerning mass transfer performance. This provides higher flexibility with respect to bioreactor equipment considered for specific processes.
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