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通过对高粘度下体积功率输入、ka值和剪切速率进行CFD计算探究摇瓶中的异相现象

Exploration of the Out-of-Phase Phenomenon in Shake Flasks by CFD Calculations of Volumetric Power Input, ka Value and Shear Rate at Elevated Viscosity.

作者信息

Dinter Carl, Gumprecht Andreas, Menze Matthias Alexander, Azizan Amizon, Hansen Sven, Büchs Jochen

机构信息

AVT - Biochemical Engineering, RWTH Aachen University, Aachen, North Rhine-Westphalia, Germany.

Evonik Operations GmbH, Hanau-Wolfgang, Hesse, Germany.

出版信息

Biotechnol Bioeng. 2025 Mar;122(3):509-524. doi: 10.1002/bit.28892. Epub 2024 Nov 30.

Abstract

Culture broth with secreted macromolecules and culture broth of filamentous fungi showing disperse growth exhibit elevated viscosity, usually with shear-thinning flow behavior. High viscosity, however, poses a serious challenge in the production and research of these compounds and organisms. It commonly causes insufficient mixing and oxygen transfer in large- and small-scale bioreactors. Computational Fluid dynamics (CFD) has been proven to be a valuable tool for the computation of important bioprocess parameters. The published literature for small-scale shaken bioreactors, especially shake flasks, however, almost exclusively focuses on water-like viscosity. In this paper, a previously published CFD model for 250 mL shake flasks was used to simulate experiments at high viscosities of up to 100 mPa·s. Compared to experimental data, the CFD model accurately predicted the liquid distribution and computed the volumetric power input with a deviation of less than 7% and the ka value within a factor of two, compared to the ka correlation from Henzler and Schedel. Furthermore, a novel approach to compute the shear rate was tested. Lastly, new insights into the out-of-phase phenomenon were gained. The presented data confirms the usefulness of the already established critical phase numbers of 0.91 and 1.26, while underlying the fundamentally smooth transition from in-phase to out-of-phase operating conditions.

摘要

含有分泌型大分子的培养液以及呈现分散生长的丝状真菌培养液具有较高的粘度,通常具有剪切变稀的流动行为。然而,高粘度在这些化合物和生物体的生产与研究中构成了严峻挑战。它通常会导致大规模和小规模生物反应器中混合不充分以及氧气传递不足。计算流体动力学(CFD)已被证明是计算重要生物过程参数的宝贵工具。然而,已发表的关于小规模摇瓶生物反应器,尤其是摇瓶的文献几乎完全集中在水状粘度上。在本文中,一个先前发表的用于250 mL摇瓶的CFD模型被用于模拟高达100 mPa·s的高粘度实验。与实验数据相比,CFD模型准确预测了液体分布,并计算了体积功率输入,其偏差小于7%,与Henzler和Schedel的ka相关性相比,ka值在两倍以内。此外,还测试了一种计算剪切速率的新方法。最后,获得了关于异相现象的新见解。所呈现的数据证实了已确立的临界相数0.91和1.26的有用性,同时揭示了从同相到异相操作条件的基本平滑过渡。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/510a/11808426/a26f27832726/BIT-122-509-g006.jpg

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