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精确发酵与同步分离策略相结合可实现高效且经济的槐糖脂生产。

Precise fermentation coupling with simultaneous separation strategy enables highly efficient and economical sophorolipids production.

作者信息

Xu Feng, Chen Yang, Zou Xiang, Chu Ju, Tian Xiwei

机构信息

State Key Laboratory of Bioreactor Engineering, East China University of Science and Technology, Shanghai 200237, China; School of Biotechnology, East China University of Science and Technology, Shanghai 200237, China.

College of Pharmaceutical Sciences, Southwest University, Chongqing 400715, China.

出版信息

Bioresour Technol. 2023 Nov;388:129719. doi: 10.1016/j.biortech.2023.129719. Epub 2023 Sep 9.

Abstract

Sophorolipids (SLs) represent highly promising biosurfactants. However, its widespread production and application encounter obstacles due to the significant costs involved. Here, an intelligent and precise regulation strategy was elucidated for the fermentation process coupled with in-situ separation production mode, to achieve cost-effective SLs production. Firstly, a mechanism-assisted data-driven model was constructed for "on-demand feeding of cells". Moreover, a strategy of step-wise oxygen supply regulation based on the demand for cell metabolic capacity was developed, which accomplished "on-demand oxygen supply of cells", to optimize the control of energy consumption. Finally, a systematic approach was implemented by integrating a semi-continuous fermentation mode with in-situ separation technology for SLs production. This strategy enhanced SLs productivity and yield, reaching 2.30 g/L/h and 0.57 g/g, respectively. These values represented a 40.2% and 18.7% increase compared to fed-batch fermentation. Moreover, the concentration of crude SLs after separation reached 793.12 g/L, facilitating downstream separation and purification processes.

摘要

槐糖脂(SLs)是极具前景的生物表面活性剂。然而,由于成本高昂,其大规模生产和应用面临障碍。在此,阐明了一种智能且精确的调控策略,用于结合原位分离生产模式的发酵过程,以实现具有成本效益的SLs生产。首先,构建了一个机制辅助的数据驱动模型用于“细胞按需补料”。此外,基于细胞代谢能力需求开发了一种逐步供氧调控策略,实现了“细胞按需供氧”,以优化能量消耗控制。最后,通过将半连续发酵模式与原位分离技术相结合,实施了一种用于SLs生产的系统方法。该策略提高了SLs的生产率和产量,分别达到2.30 g/L/h和0.57 g/g。与分批补料发酵相比,这些值分别提高了40.2%和18.7%。此外,分离后粗SLs的浓度达到793.12 g/L,便于下游的分离和纯化过程。

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