Hild H M, Stuckey D C, Leak D J
Department of Chemical Engineering, Imperial College of Science, Technology and Medicine, South Kensington, London SW7 2AZ, UK.
Appl Microbiol Biotechnol. 2003 Feb;60(6):679-86. doi: 10.1007/s00253-002-1175-5. Epub 2002 Dec 19.
Thermoanaerobacter ethanolicus JW200 Fe(7) was grown in continuous culture, using xylose as the primary carbon source, with progressively lower concentrations of supplementary yeast extract. This enabled the comparison of metabolic flux to fermentation end-products under carbon-limited and carbon-sufficient (yeast extract-limited) conditions and the determination of process data under fully mass-balanced conditions. Under carbon-limitation, the specific ethanol-formation rate was described by q (p)=40.34 micro +3.74, the specific rate of substrate utilisation for maintenance was 0.31+/-0.02 g x g(-1) x h(-1) and the maximum cell yield on xylose, corrected for maintenance requirements, was 0.15+/-0.04 g x g(-1). Based on the product profiles, these corresponded to a maintenance coefficient of m(ATP)=4.1+/-0.5 mmol x g(-1) x h(-1) and a maximum cell yield of = 14.7+/-0.8 x g x mol(-1). Limitation by a component in yeast extract resulted in incomplete xylose utilisation, increased catabolic flux rates (primarily resulting in increased lactate production, due to limitations in the flux through the phosphoroclastic reaction), a reduction in cell yield = 10.0+/-1.0 g x mol(-1) and an increase in maintenance energy requirements of m(ATP)=7.95+/-0.7 mmol x g(-1). The latter was also reflected in a shift from ethanol to acetate production at lower growth rates. An analysis of ethanol and acetate tolerance indicated that any high-intensity process employing this strain would require a bioreactor design which incorporated continuous ethanol stripping.
嗜热栖热放线菌JW200 Fe(7)在连续培养中生长,以木糖作为主要碳源,并逐步降低补充酵母提取物的浓度。这使得能够比较在碳限制和碳充足(酵母提取物限制)条件下代谢通量与发酵终产物的关系,并在完全质量平衡条件下确定过程数据。在碳限制条件下,特定乙醇形成速率由q(p)=40.34微+3.74描述,用于维持的底物利用特定速率为0.31±0.02 g x g(-1) x h(-1),校正维持需求后木糖上的最大细胞产率为0.15±0.04 g x g(-1)。根据产物谱,这些对应于维持系数m(ATP)=4.1±0.5 mmol x g(-1) x h(-1)和最大细胞产率=14.7±0.8 x g x mol(-1)。酵母提取物中一种成分的限制导致木糖利用不完全,分解代谢通量速率增加(主要导致乳酸产量增加,这是由于通过磷酸解反应的通量受限),细胞产率降低=10.0±1.0 g x mol(-1),维持能量需求增加至m(ATP)=7.95±0.7 mmol x g(-1)。后者也反映在较低生长速率下从乙醇生产向乙酸生产的转变。对乙醇和乙酸耐受性的分析表明,任何采用该菌株的高强度过程都需要一种包含连续乙醇汽提的生物反应器设计。