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采用阶段控制发酵和降黏策略提高枯草芽孢杆菌聚-γ-谷氨酸的产量。

Enhanced Production of Poly-γ-glutamic Acid by Bacillus subtilis Using Stage-controlled Fermentation and Viscosity Reduction Strategy.

机构信息

State Key Laboratory for Conservation and Utilization of Subtropical Agro-bioresources, Guangxi Microorganism and Enzyme Research Center of Engineering Technology, College of Life Science and Technology, Guangxi University, 100 Daxue Road, Nanning, 530004, Guangxi, China.

Key Laboratory of Biochemistry and Molecular Biology (Guilin Medical University), Education Department of Guangxi Zhuang Autonomous Region, School of Intelligent Medicine and Biotechnology, Guilin Medical University, 1 Zhiyuan Road, Guilin, 541199, Guangxi, China.

出版信息

Appl Biochem Biotechnol. 2024 Mar;196(3):1527-1543. doi: 10.1007/s12010-023-04644-1. Epub 2023 Jul 11.

Abstract

In this study, the production of poly-γ-glutamic acid (PGA) by Bacillus subtilis using stage-controlled fermentation and viscosity reduction strategy was investigated in detail. Based on the single-factor optimization experiment, temperature (42 °C and 37 °C), pH (7.0 and uncontrolled), aeration rate (1.2 vvm and 1.0 vvm), and agitation speed (700 rpm and 500 rpm) were selected for the two-stage controlled fermentation (TSCF). The time points for the TSCF of temperature, pH, aeration rate, and agitation speed were set at 18.52 h, 2.82 h, 5.92 h, and 3.62 h, respectively, based on the kinetic analysis. A PGA titer of 19.79 ~ 22.17 g/L was obtained from the TSCF, which did not increase significantly than that (21.25 ± 1.26 g/L) of non-stage controlled fermentation (NSCF). This may be due to the high viscosity and low dissolved oxygen of the PGA fermentation broth. Thus, the TSCF combined with a viscosity reduction strategy was developed to further improve the production of PGA. The PGA titer reached 25.00 ~ 30.67 g/L, which increased by 17.66 ~ 32.94% to that of NSCF. This study provided a valuable reference for the development of process control strategies for high-viscosity fermentation systems.

摘要

在这项研究中,详细研究了枯草芽孢杆菌通过阶段控制发酵和降粘策略生产聚-γ-谷氨酸(PGA)。基于单因素优化实验,选择温度(42°C 和 37°C)、pH(7.0 和未控制)、通气速率(1.2 vvm 和 1.0 vvm)和搅拌速度(700 rpm 和 500 rpm)进行两阶段控制发酵(TSCF)。根据动力学分析,TSCF 的温度、pH、通气速率和搅拌速度的时间点分别设置为 18.52 h、2.82 h、5.92 h 和 3.62 h。通过 TSCF 获得了 19.79 ~ 22.17 g/L 的 PGA 产量,与非阶段控制发酵(NSCF)的产量(21.25 ± 1.26 g/L)相比没有显著增加。这可能是由于 PGA 发酵液的高粘度和低溶解氧所致。因此,开发了 TSCF 结合降粘策略,以进一步提高 PGA 的产量。PGA 产量达到 25.00 ~ 30.67 g/L,与 NSCF 相比提高了 17.66 ~ 32.94%。本研究为高粘度发酵系统的过程控制策略的发展提供了有价值的参考。

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