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Fed-batch production of MCL-PHA with elevated 3-hydroxynonanoate content

机译:3-羟基壬酸含量提高的MCL-PHA的分批补料生产

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摘要

With no inhibition of β-oxidation, Pseudomonas putida KT2440 produces medium-chain-length poly(3-hydroxyalkanoate) (MCL-PHA) with approximately 65 mol% 3-hydroxynonanoate (HN) from nonanoic acid. Production of PHA with higher HN content and an adjustable monomeric composition was obtained using acrylic acid, a fatty acid β-oxidation inhibitor, together with nonanoic acid and glucose as co-substrates in fed-batch fermentations. Different monomeric compositions were obtained by varying the feeding conditions to impose different specific growth rates and inhibitor feed concentrations. At a nonanoic acid: glucose: acrylic acid feed mass ratio of 1.25: 1: 0.05 and a specific growth rate of 0.15 h-1, 71.4 g L-1 biomass was produced containing 75.5% PHA with 89 mol% HN at a cumulative PHA productivity of 1.8 g L-1 h-1.
机译:在不抑制β氧化的情况下,恶臭假单胞菌KT2440可以从壬酸生产中链长度的聚(3-羟基链烷酸酯)(MCL-PHA)和约65mol%的3-羟基壬酸酯(HN)。在补料分批发酵中,使用丙烯酸,脂肪酸β-氧化抑制剂,壬酸和葡萄糖作为共底物,可以生产具有较高HN含量和可调节单体组成的PHA。通过改变进料条件以施加不同的比生长速率和抑制剂进料浓度获得不同的单体组成。在壬酸:葡萄糖:丙烯酸的进料质量比为1.25:1:0.05且比生长速率为0.15h -1 时,生物量为71.4 g L -1 生产的产品中含有75.5%的PHA和89mol%的HN,累计PHA生产率为1.8 g L -1 h -1

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