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肺炎克雷伯氏菌对生物柴油副产甘油的代谢:兼氧和缺氧条件下不同进料速率下的代谢产物池。

Biodiesel residual glycerol metabolism by Klebsiella pneumoniae: pool of metabolites under anaerobiosis and oxygen limitation as a function of feeding rates.

机构信息

Biotechnology & Biochemical Engineering Laboratory (BiotecLab), Federal University of Rio Grande do Sul, Av. Bento Gonçalves 9500, Porto Alegre, Rio Grande do Sul, Brazil.

出版信息

Appl Biochem Biotechnol. 2013 Mar;169(6):1952-64. doi: 10.1007/s12010-013-0114-5. Epub 2013 Jan 26.

Abstract

The metabolism of residual glycerol from biodiesel synthesis by Klebsiella pneumoniae BLh-1 was investigated in this study. Batch and fed-batch cultivations were performed in bioreactors under anaerobic and oxygen limitation conditions. Results of batch cultivations showed that the main product was 1,3-propanediol (1,3-PD) in both conditions, although the higher yields and productivities (0.46 mol mol(-1) glycerol and 1.22 g L(-1) h(-1), respectively) were obtained under anaerobic condition. Large amounts of ethanol were also produced under batch anaerobic condition, peaking at 12.30 g L(-1). Batch cultivations under oxygen limitation were characterized by faster growth kinetics, with higher biomass production but lower conversions of glycerol into 1,3-PD, with yields and productivities of 0.33 mol mol(-1) glycerol and 0.99 g L(-1) h(-1), respectively. The fed-batch cultivations were carried out in order to investigate the effects of feeding of raw glycerol on cells. Fed-batch under anaerobiosis showed that 1,3-PD and ethanol concentrations increased with the feeding rate, with maximal productions of 26.12 and 19.2 g L(-1), respectively. The oxygen limitation conditions diverted the bacterium metabolism to an elevated lactic acid formation, reaching 59 g L(-1) in higher feeding rates of glycerol, but lowering the production of ethanol.

摘要

本研究考察了肺炎克雷伯氏菌 BLh-1 对生物柴油合成中残留甘油的代谢。在厌氧和缺氧条件下,在生物反应器中进行分批和补料分批培养。分批培养的结果表明,尽管在厌氧条件下分别获得了更高的产率和生产率(0.46 mol mol(-1)甘油和 1.22 g L(-1) h(-1)),但两种条件下的主要产物均为 1,3-丙二醇(1,3-PD)。在分批厌氧条件下也产生了大量的乙醇,最高达到 12.30 g L(-1)。缺氧条件下的分批培养以更快的生长动力学为特征,具有更高的生物量产量,但甘油转化为 1,3-PD 的转化率较低,产率和生产率分别为 0.33 mol mol(-1)甘油和 0.99 g L(-1) h(-1)。进行补料分批培养是为了研究原料甘油补料对细胞的影响。在厌氧条件下进行补料分批培养时,随着进料速率的增加,1,3-PD 和乙醇浓度均增加,最大产量分别为 26.12 和 19.2 g L(-1)。在缺氧条件下,限制氧气的条件使细菌代谢转向乳酸的形成增加,在较高的甘油进料速率下达到 59 g L(-1),但降低了乙醇的产量。

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