Allaart Maximilienne T, Korkontzelos Charilaos, Sousa Diana Z, Kleerebezem Robbert
Department of Biotechnology, Delft University of Technology, Delft, The Netherlands.
Laboratory of Microbiology, Wageningen University & Research, Wageningen, Netherlands.
Biotechnol Bioeng. 2024 Apr;121(4):1325-1335. doi: 10.1002/bit.28652. Epub 2024 Jan 24.
Syngas fermentation has gained momentum over the last decades. The cost-efficient design of industrial-scale bioprocesses is highly dependent on quantitative microbial growth data. Kinetic and stoichiometric models for syngas-converting microbes exist, but accurate experimental validation of the derived parameters is lacking. Here, we describe a novel experimental approach for measuring substrate uptake kinetics of gas-fermenting microbes using the model microorganism Clostridium autoethanogenum. One-hour disturbances of a steady-state chemostat bioreactor with increased CO partial pressures (up to 1.2 bar) allowed for measurement of biomass-specific CO uptake- and CO production rates ( , ) using off-gas analysis. At a p of 1.2 bar, a of -119 ± 1 mmol g h was measured. This value is 1.8-3.5-fold higher than previously reported experimental and kinetic modeling results for syngas fermenters. Analysis of the catabolic flux distribution reveals a metabolic shift towards ethanol production at the expense of acetate at p 0.6 atm, likely to be mediated by acetate availability and cellular redox state. We characterized this metabolic shift as acetogenic overflow metabolism. These results provide key mechanistic understanding of the factors steering the product spectrum of CO fermentation in C. autoethanogenum and emphasize the importance of dedicated experimental validation of kinetic parameters.
在过去几十年里,合成气发酵发展迅速。工业规模生物过程的经济高效设计高度依赖于定量的微生物生长数据。虽然存在用于合成气转化微生物的动力学和化学计量模型,但缺乏对推导参数的准确实验验证。在此,我们描述了一种使用模式微生物自养乙醇梭菌来测量气体发酵微生物底物摄取动力学的新型实验方法。通过将稳态恒化器生物反应器在1小时内的CO分压提高(高达1.2巴)进行扰动,利用尾气分析来测量生物质特异性CO摄取率和CO产生率( , )。在1.2巴的p值下,测得 为-119±1毫摩尔克⁻¹小时⁻¹。该值比先前报道的合成气发酵罐的实验和动力学建模结果高1.8至3.5倍。对分解代谢通量分布的分析表明,在p≥0.6大气压时,代谢向以乙酸为代价的乙醇生产转变,这可能由乙酸可用性和细胞氧化还原状态介导。我们将这种代谢转变表征为产乙酸溢流代谢。这些结果为指导自养乙醇梭菌中CO发酵产物谱的因素提供了关键的机理理解,并强调了对动力学参数进行专门实验验证的重要性。