A General Process-Based Model for Describing the Metabolic Shift in Microbial Cell Cultures

被引:4
|
作者
Carteni, Fabrizio [1 ]
Occhicone, Alessio [1 ,2 ]
Giannino, Francesco [1 ]
Vincenot, Christian E. [3 ]
de Alteriis, Elisabetta [4 ]
Palomba, Emanuela [1 ,5 ]
Mazzoleni, Stefano [1 ]
机构
[1] Univ Naples Federico II, Dept Agr Sci, Portici, Italy
[2] Univ Naples Parthenope, Dept Engn, Naples, Italy
[3] Kyoto Univ, Dept Social Informat, Kyoto, Japan
[4] Univ Naples Federico II, Dept Biol, Naples, Italy
[5] Staz Zool Anton Dohrn, Sect Res Infrastruct Marine Biol Resources, Naples, Italy
来源
FRONTIERS IN MICROBIOLOGY | 2020年 / 11卷
关键词
Escherichia coli; Bacillus subtilis; System Dynamics (SD) model; self-inhibition; high cell-density culture; overflow metabolism; Crabtree; Warburg effect; RECOMBINANT PROTEIN-PRODUCTION; FED-BATCH CULTURES; ESCHERICHIA-COLI; DENSITY CULTIVATION; SACCHAROMYCES-CEREVISIAE; OVERFLOW METABOLISM; BACILLUS-SUBTILIS; CARBON FLUX; GROWTH; ACETATE;
D O I
10.3389/fmicb.2020.521368
中图分类号
Q93 [微生物学];
学科分类号
071005 ; 100705 ;
摘要
The metabolic shift between respiration and fermentation at high glucose concentration is a widespread phenomenon in microbial world, and it is relevant for the biotechnological exploitation of microbial cell factories, affecting the achievement of high-cell-densities in bioreactors. Starting from a model already developed for the yeastSaccharomyces cerevisiae, based on the System Dynamics approach, a general process-based model for two prokaryotic species of biotechnological interest, such asEscherichia coliandBacillus subtilis, is proposed. The model is based on the main assumption that glycolytic intermediates act as central catabolic hub regulating the shift between respiratory and fermentative pathways. Furthermore, the description of a mixed fermentation with secondary by-products, characteristic of bacterial metabolism, is explicitly considered. The model also represents the inhibitory effect on growth and metabolism of self-produced toxic compounds relevant in assessing the late phases of high-cell density culture. Model simulations reproduced data from experiments reported in the literature with different strains of non-recombinant and recombinantE. coliandB. subtiliscultured in both batch and fed-batch reactors. The proposed model, based on simple biological assumptions, is able to describe the main dynamics of two microbial species of relevant biotechnological interest. It demonstrates that a reductionist System Dynamics approach to formulate simplified macro-kinetic models can provide a robust representation of cell growth and accumulation in the medium of fermentation by-products.
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页数:12
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