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在以棕榈油为碳源的发酵过程中,分批和补料分批培养方式对鞘氨醇单胞菌 PBD-410L 生产脂肽生物表面活性剂的影响。

Production of lipopeptide biosurfactant in batch and fed-batch Streptomyces sp. PBD-410L cultures growing on palm oil.

机构信息

School of Biological Sciences, Universiti Sains Malaysia, 11800, Penang, Malaysia.

出版信息

Bioprocess Biosyst Eng. 2021 Jul;44(7):1577-1592. doi: 10.1007/s00449-021-02543-5. Epub 2021 Mar 9.

Abstract

The present study focused on lipopeptide biosurfactant production by Streptomyces sp. PBD-410L in batch and fed-batch fermentation in a 3-L stirred-tank reactor (STR) using palm oil as a sole carbon source. In batch cultivation, the impact of bioprocessing parameters, namely aeration rate and agitation speed, was studied to improve biomass growth and lipopeptide biosurfactant production. The maximum oil spreading technique (OST) result (45 mm) which corresponds to 3.74 g/L of biosurfactant produced, was attained when the culture was agitated at 200 rpm and aeration rate of 0.5 vvm. The best aeration rate and agitation speed obtained from the batch cultivation was adopted in the fed-batch cultivation using DO-stat feeding strategy to further improve the lipopeptide biosurfactant production. The lipopeptide biosurfactant production was enhanced from 3.74 to 5.32 g/L via fed-batch fermentation mode at an initial feed rate of 0.6 mL/h compared to that in batch cultivation. This is the first report on the employment of fed-batch cultivation on the production of biosurfactant by genus Streptomyces.

摘要

本研究采用棕榈油作为唯一碳源,在 3-L 搅拌釜式反应器(STR)中,通过分批和补料分批发酵的方式,研究了链霉菌 PBD-410L 产生脂肽生物表面活性剂。在分批培养中,研究了生物工艺参数,即通气速率和搅拌速度,以提高生物量生长和脂肽生物表面活性剂的生产。最大油扩散技术(OST)结果(45 毫米)对应于 3.74 克/升的生物表面活性剂产量,当培养物以 200 rpm 搅拌和 0.5 vvm 的通气速率时达到。从分批培养中获得的最佳通气速率和搅拌速度被采用在补料分批培养中,使用 DO-stat 进料策略进一步提高脂肽生物表面活性剂的生产。与分批培养相比,通过补料分批发酵模式,初始进料速率为 0.6 mL/h,脂肽生物表面活性剂的产量从 3.74 克/升提高到 5.32 克/升。这是首次报道在链霉菌属生产生物表面活性剂时采用补料分批培养。

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