首页> 美国卫生研究院文献>Applied and Environmental Microbiology >Poly(3-Hydroxybutyrate) Production from Glycerol by Zobellella denitrificans MW1 via High-Cell-Density Fed-Batch Fermentation and Simplified Solvent Extraction
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Poly(3-Hydroxybutyrate) Production from Glycerol by Zobellella denitrificans MW1 via High-Cell-Density Fed-Batch Fermentation and Simplified Solvent Extraction

机译:反硝化细菌MW1通过高细胞密度补料分批发酵和简化的溶剂萃取法从甘油生产聚(3-羟基丁酸)

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摘要

Industrial production of biodegradable polyesters such as polyhydroxyalkanoates is hampered by high production costs, among which the costs for substrates and for downstream processing represent the main obstacles. Inexpensive fermentable raw materials such as crude glycerol, an abundant by-product of the biodiesel industry, have emerged to be promising carbon sources for industrial fermentations. In this study, Zobellella denitrificans MW1, a recently isolated bacterium, was used for the production of poly(3-hydroxybutyrate) (PHB) from glycerol as the sole carbon source. Pilot-scale fermentations (42-liter scale) were conducted to scale up the high PHB accumulation capability of this strain. By fed-batch cultivation, at first a relatively high cell density (29.9 ± 1.3 g/liter) was obtained during only a short fermentation period (24 h). However, the PHB content was relatively low (31.0% ± 4.2% [wt/wt]). Afterwards, much higher concentrations of PHB (up to 54.3 ± 7.9 g/liter) and higher cell densities (up to 81.2 ± 2.5 g/liter) were obtained by further fed-batch optimization in the presence of 20 g/liter NaCl, with optimized feeding of glycerol and ammonia to support both cell growth and polymer accumulation over a period of 50 h. A high specific growth rate (0.422/h) and a short doubling time (1.64 h) were attained. The maximum PHB content obtained was 66.9% ± 7.6% of cell dry weight, and the maximum polymer productivity and substrate yield coefficient were 1.09 ± 0.16 g/liter/h and 0.25 ± 0.04 g PHB/g glycerol, respectively. Furthermore, a simple organic solvent extraction process was employed for PHB recovery during downstream processing: self-flotation of cell debris after extraction of PHB with chloroform allowed a convenient separation of a clear PHB-solvent solution from the cells. Maximum PHB recovery (85.0% ± 0.10% [wt/wt]) was reached after 72 h of extraction with chloroform at 30°C, with a polymer purity of 98.3% ± 1.3%.
机译:高生产成本阻碍了可生物降解聚酯(如聚羟基链烷酸酯)的工业生产,其中底物和下游加工的成本是主要障碍。廉价的可发酵原料,例如粗甘油,是生物柴油工业的丰富副产品,已成为有希望的工业发酵碳源。在这项研究中,最近分离出的细菌Zobellella denitrificans MW1被用于由甘油作为唯一碳源生产聚(3-羟基丁酸酯)(PHB)。进行中试发酵(42升规模)以扩大该菌株的高PHB积累能力。通过分批补料培养,首先仅在很短的发酵阶段(24小时)就获得了较高的细胞密度(29.9±1.3 g /升)。但是,PHB含量相对较低(31.0%±4.2%[wt / wt])。之后,通过在20 g /升NaCl存在下进一步进料分批优化,获得了更高浓度的PHB(最高54.3±7.9 g /升)和更高的细胞密度(最高81.2±2.5 g /升)。优化了甘油和氨的进料,以在50小时内支持细胞生长和聚合物积累。获得了较高的比生长速率(0.422 / h)和较短的加倍时间(1.64 h)。获得的最大PHB含量为细胞干重的66.9%±7.6%,最大聚合物生产率和底物产率系数分别为1.09±0.16 g / l / h和0.25±0.04 g PHB / g甘油。此外,在下游处理过程中,采用了一种简单的有机溶剂提取工艺来回收PHB:用氯仿提取PHB后,细胞碎片的自浮选可以方便地从细胞中分离出清晰的PHB溶剂溶液。在30°C下用氯仿萃取72小时后,达到了最大的PHB回收率(85.0%±0.10%[wt / wt]),聚合物纯度为98.3%±1.3%。

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