Simulated oxygen and glucose gradients as a prerequisite for predicting industrial scale performance a priori

被引:29
作者
Kuschel, Maike [1 ]
Takors, Ralf [1 ]
机构
[1] Univ Stuttgart, Inst Biochem Engn, Allmandring 31, D-70569 Stuttgart, Germany
关键词
cellular lifelines; CFD; double gradient; stirred tank; POPULATION BALANCE; ESCHERICHIA-COLI; MASS-TRANSFER; STIRRED-TANK; DRAG COEFFICIENTS; MODEL; VALIDATION; BIOREACTOR; FLOW; COMPARTMENT;
D O I
10.1002/bit.27457
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Transferring bioprocesses from lab to industrial scale without loss of performance is key for the successful implementation of novel production approaches. Because mixing and mass transfer is usually hampered in large scale, cells experience heterogeneities eventually causing deteriorated yields, that is, reduced titers, productivities, and sugar-to-product conversions. Accordingly, reliable and easy-to-implement tools for a priori prediction of large-scale performance based on dry and wet-lab tests are heavily needed. This study makes use of computational fluid dynamic simulations of a multiphase multi-impeller stirred tank in pilot scale. So-calledlifelines, records of 120,000Corynebacterium glutamicumcells experiencing fluctuating environmental conditions, were identified and used to properly design wet-lab scale-down (SD) devices. Physical parameters such as power input, gas hold up,kLa, and mixing time showed good agreement with experimental measurements. Analyzing the late fed-batch cultivation revealed that the complex double gradient of glucose and oxygen can be translated into a wet-lab SD setup with only few compartments. Most remarkably, the comparison of different mesh sizes outlined that even the coarsest approach with a mesh density of1.12x105#/m3was sufficient to properly predict physical and biological readouts. Accordingly, the approach offers the potential for the thorough analysis of realistic industrial case scenarios.
引用
收藏
页码:2760 / 2770
页数:11
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