首页> 外文期刊>Journal of Biotechnology >Increasing the yield of MCL-PHA from nonanoic acid by co-feeding glucose during the PHA accumulation stage in two-stage fed-batch fermentations of Pseudomonas putida KT2440
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Increasing the yield of MCL-PHA from nonanoic acid by co-feeding glucose during the PHA accumulation stage in two-stage fed-batch fermentations of Pseudomonas putida KT2440

机译:在恶臭假单胞菌KT2440的两阶段分批补料分批发酵中,通过在PHA积累阶段共补料葡萄糖来提高壬酸的MCL-PHA产量

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摘要

A method was developed to increase the yield of MCL-PHA from nonanoic acid in the PHA accumulation phase. Pseudomonas putida KT2440 was grown on glucose until ammonium-limitation was imposed. In the second (accumulation) stage, either glucose, nonanoic acid, or a mixture of these carbon and energy sources was supplied. Since the medium-chain-length poly-3-hydroxyalkanoate (MCL-PHA) subunits produced are unique for each carbon source, their relative contribution to PHA yield could be calculated. Y(C7+C9)/NA was 0.254 mol mol(-1) during PHA synthesis from nonanoic acid. Y(C8+C10)/G was only 0.057 mol mol(-1) during PHA synthesis from glucose. When nonanoic acid and glucose were fed together, Y(C7+C8)/NA almost doubled to 0.450 mol mol(-1) while Y(C8+C10)/G decreased to 0.011 mol mol(-1). These results demonstrate that substantial savings can be obtained by feeding glucose with substrates that are good for PHA production but much more expensive than glucose.
机译:开发了一种在PHA积累阶段提高壬酸MCL-PHA收率的方法。恶臭假单胞菌KT2440在葡萄糖上生长直至施加铵限制。在第二(累积)阶段,提供葡萄糖,壬酸或这些碳源和能源的混合物。由于产生的中链长度聚3-羟基链烷酸酯(MCL-PHA)亚基对于每个碳源都是唯一的,因此可以计算出它们对PHA产量的相对贡献。从壬酸合成PHA期间,Y(C7 + C9)/ NA为0.254 mol mol(-1)。在从葡萄糖合成PHA期间,Y(C8 + C10)/ G仅为0.057 mol mol(-1)。当壬酸和葡萄糖一起喂入时,Y(C7 + C8)/ NA几乎翻倍至0.450 mol mol(-1),而Y(C8 + C10)/ G降至0.011 mol -1(mol)。这些结果表明,通过向葡萄糖供给对PHA产生有益但比葡萄糖贵得多的底物,可以大大节省成本。

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