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基于溶解氧优化结合 pH 控制和农杆菌 sp. ATCC 31749 代谢特性的凝乳酶发酵工艺改进。

Improved curdlan fermentation process based on optimization of dissolved oxygen combined with pH control and metabolic characterization of Agrobacterium sp. ATCC 31749.

机构信息

Key Laboratory of Industrial Biotechnology of Ministry of Education, School of Biotechnology, Jiangnan University, Wuxi, China.

出版信息

Appl Microbiol Biotechnol. 2012 Jan;93(1):367-79. doi: 10.1007/s00253-011-3448-3. Epub 2011 Jul 8.

DOI:10.1007/s00253-011-3448-3
PMID:21739265
Abstract

A significant problem in scale-down cultures, rarely studied for metabolic characterization and curdlan-producing Agrobacterium sp. ATCC 31749, is the presence of dissolved oxygen (DO) gradients combined with pH control. Constant DO, between 5% and 75%, was maintained during batch fermentations by manipulating the agitation with PID system. Fermentation, metabolic and kinetic characterization studies were conducted in a scale-down system. The curdlan yield, intracellular nucleotide levels and glucose conversion efficiency into curdlan were significantly affected by DO concentrations. The optimum DO concentrations for curdlan production were 45-60%. The average curdlan yield, curdlan productivity and glucose conversion efficiency into curdlan were enhanced by 80%, 66% and 32%, respectively, compared to that at 15% DO. No apparent difference in the gel strength of the resulting curdlan was detected. The comparison of curdlan biosynthesis and cellular nucleotide levels showed that curdlan production had positive relationship with intracellular levels of UTP, ADP, AMP, NAD(+), NADH and UDP-glucose. The curdlan productivity under 45% DO and 60% DO was different during 20-50 h. However, after 60 h curdlan productivity of both conditions was similar. On that basis, a simple and reproducible two-stage DO control process for curdlan production was developed. Curdlan production yield reached 42.8 g/l, an increase of 30% compared to that of the single agitation speed control process.

摘要

在规模缩小的培养物中,存在溶解氧 (DO) 梯度与 pH 控制相结合的问题,这是一个重大问题,对于代谢特征研究和产胶链霉菌 ATCC 31749 来说很少研究。在分批发酵过程中,通过使用 PID 系统来控制搅拌,使 DO 保持在 5%到 75%之间的恒定水平。在缩小规模的系统中进行了发酵、代谢和动力学特征研究。胶聚糖产量、细胞内核苷酸水平和葡萄糖转化为胶聚糖的效率受到 DO 浓度的显著影响。胶聚糖生产的最佳 DO 浓度为 45-60%。与 15% DO 相比,胶聚糖产量、胶聚糖生产力和葡萄糖转化为胶聚糖的效率分别提高了 80%、66%和 32%。所得胶聚糖的凝胶强度没有明显差异。胶聚糖生物合成和细胞内核苷酸水平的比较表明,胶聚糖生产与 UTP、ADP、AMP、NAD(+)、NADH 和 UDP-葡萄糖的细胞内水平呈正相关。在 45% DO 和 60% DO 下,20-50 h 时的胶聚糖生产力不同。然而,60 h 后,两种条件下的胶聚糖生产力相似。在此基础上,开发了一种简单且可重复的两阶段 DO 控制工艺,用于胶聚糖生产。胶聚糖产量达到 42.8 g/L,与单一搅拌速度控制工艺相比提高了 30%。

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