Physiological Response of Penicillium chrysogenum to Mimicked Local and Global Perturbations of Substrate and Dissolved Oxygen Gradients at Industrial-Scale

IF 3.5 2区 生物学 Q2 BIOTECHNOLOGY & APPLIED MICROBIOLOGY
Yining Chen, Cees Haringa, Zejian Wang, Yingping Zhuang, Guan Wang
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Abstract

Industrial-scale microbial fermentation processes often face limitations in mixing and mass transfer, leading to the formation of environmental gradients within the bioreactor. These gradients expose microbes to heterogeneous conditions over time and space. In this study, we evaluated the effects of combined substrate and dissolved oxygen (DO) gradients on the metabolic response of Penicillium chrysogenum at an industrial scale. Three representative heterogeneous environments were simulated in scale-down systems: (1) feed inlet (high glucose, low oxygen (HGLO): CS > 20 mM, DO < 0.012 mM), (2) aeration inlet (high oxygen, low glucose (HOLG): CS < 0.8 mM, DO > 0.2 mM), and (3) global environment (periodic 360 s fluctuation cycle with 45 s of HGLO and 75 s of HOLG conditions). Results showed that prolonged exposure to feed inlet conditions led to a complete loss of penicillin production capacity, accompanied by significant excretion of intracellular metabolites, and this effect was largely irreversible. While, cells randomly walking under the top impeller zone did not lose production capacity but showed signs of premature degeneration due to increased energy demand. When exposed to the global environment, cells finely tuned their metabolism in a periodical manner, with nearly a 50% loss of penicillin productivity. In summary, substrate gradients alone did not cause irreversible effects, but large substrate gradients contributed to reduced productivity. Oxygen gradients, however, not only reduced production but also caused irreversible cellular damage. These findings provide valuable insights for developing scale-up criteria and strain engineering strategies aimed at improving large-scale culture performance.

Abstract Image

工业规模下青霉菌对模拟底物和溶解氧梯度局部和全局扰动的生理反应
工业规模的微生物发酵过程经常面临混合和传质的限制,导致生物反应器内形成环境梯度。这些梯度使微生物在不同的时间和空间条件下暴露。在本研究中,我们评估了复合底物和溶解氧(DO)梯度对工业规模青霉菌代谢反应的影响。在按比例缩小的系统中模拟了三种具有代表性的异质环境:(1)进料口(高氧低氧(HGLO): CS < 20 mM, DO < 0.012 mM),(2)曝气口(高氧低氧(HOLG): CS < 0.8 mM, DO > 0.2 mM),(3)全局环境(周期性360 s波动周期,HGLO 45 s, HOLG 75 s)。结果表明,长期暴露在进料条件下会导致青霉素生产能力完全丧失,并伴有细胞内代谢物的大量排泄,而且这种影响在很大程度上是不可逆的。然而,随机行走在顶部叶轮区域下的细胞没有失去生产能力,但由于能量需求增加而表现出过早退化的迹象。当暴露在全球环境中时,细胞以一种周期性的方式精细地调节它们的新陈代谢,青霉素的生产力损失了近50%。综上所述,基材梯度本身不会造成不可逆的影响,但大的基材梯度会导致生产率降低。然而,氧梯度不仅减少了生产,而且造成了不可逆的细胞损伤。这些发现为开发规模放大标准和应变工程策略提供了有价值的见解,旨在提高大规模培养性能。
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来源期刊
Biotechnology and Bioengineering
Biotechnology and Bioengineering 工程技术-生物工程与应用微生物
CiteScore
7.90
自引率
5.30%
发文量
280
审稿时长
2.1 months
期刊介绍: Biotechnology & Bioengineering publishes Perspectives, Articles, Reviews, Mini-Reviews, and Communications to the Editor that embrace all aspects of biotechnology. These include: -Enzyme systems and their applications, including enzyme reactors, purification, and applied aspects of protein engineering -Animal-cell biotechnology, including media development -Applied aspects of cellular physiology, metabolism, and energetics -Biocatalysis and applied enzymology, including enzyme reactors, protein engineering, and nanobiotechnology -Biothermodynamics -Biofuels, including biomass and renewable resource engineering -Biomaterials, including delivery systems and materials for tissue engineering -Bioprocess engineering, including kinetics and modeling of biological systems, transport phenomena in bioreactors, bioreactor design, monitoring, and control -Biosensors and instrumentation -Computational and systems biology, including bioinformatics and genomic/proteomic studies -Environmental biotechnology, including biofilms, algal systems, and bioremediation -Metabolic and cellular engineering -Plant-cell biotechnology -Spectroscopic and other analytical techniques for biotechnological applications -Synthetic biology -Tissue engineering, stem-cell bioengineering, regenerative medicine, gene therapy and delivery systems The editors will consider papers for publication based on novelty, their immediate or future impact on biotechnological processes, and their contribution to the advancement of biochemical engineering science. Submission of papers dealing with routine aspects of bioprocessing, description of established equipment, and routine applications of established methodologies (e.g., control strategies, modeling, experimental methods) is discouraged. Theoretical papers will be judged based on the novelty of the approach and their potential impact, or on their novel capability to predict and elucidate experimental observations.
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