Department of Chemical Engineering, Massachusetts Institute of Technology, Biotechnology Process Engineering Center, Cambridge, Massachusetts 02139, USA.
Biotechnol Bioeng. 1991 Jan 5;37(1):80-92. doi: 10.1002/bit.260370112.
Axial and radial oxygen depletion are believed to be critical scale-limiting factors in the design of cell culture hollow fiber bioreactors. A mathematical analysis of oxygen depletion has been performed in order to develop effectiveness factor plots to aid in the scaling of hollow fiber bioreactors with cells immobilized in the shell-side. Considerations of the lumen mass transport resistances and the axial gradients were added to previous analyses of this immobilization geometry. An order of magnitude analysis was used to evaluate the impact of the shell-side convective fluxes on the oxygen transport. A modified Thiele modulus and a lumen and membrane resistance factor have been derived from the model. Use of these terms in the effectiveness factor plots results in a considerable simplification of the presentation and use of the model. Design criteria such as fiber dimensions and spacing, reactor lengths, and recycle flow rates can be selected using these plots. Model predictions of the oxygen limitations were compared to experimental measurements of the axial cell distributions in a severely oxygen limited hollow fiber bioreactor. Despite considerable uncertainty in our parameters and nonidealities in hollow fiber geometry, the cell distribution correlated well with the modeling results.
轴向和径向氧耗被认为是细胞培养中空纤维生物反应器设计中关键的限制因素。为了开发效能因子图以帮助对固定在壳侧的细胞的中空纤维生物反应器进行缩放,已经对氧耗进行了数学分析。考虑到腔室质量传递阻力和轴向梯度,对该固定化几何形状的先前分析进行了补充。使用量级分析来评估壳侧对流通量对氧气传输的影响。从模型中推导出了修正的 Thiele 模量和腔室及膜阻力因子。在效能因子图中使用这些术语可大大简化模型的呈现和使用。可以使用这些图选择纤维尺寸和间距、反应器长度和再循环流速等设计标准。尽管我们的参数存在相当大的不确定性并且中空纤维几何形状不理想,但细胞分布与建模结果很好地相关。