首页> 外文OA文献 >Entwicklung und Anwendung einer Fed-batch-Betriebsweise mit Nährstofffreisetzungssystemen zur kontrollierten Kultivierung und zum Screening von Mikroorganismen in Schüttelreaktoren
【2h】

Entwicklung und Anwendung einer Fed-batch-Betriebsweise mit Nährstofffreisetzungssystemen zur kontrollierten Kultivierung und zum Screening von Mikroorganismen in Schüttelreaktoren

机译:具有营养释放系统的分批分批操作模式的开发和应用,用于控制培养和振动筛反应器中的微生物筛选

代理获取
本网站仅为用户提供外文OA文献查询和代理获取服务,本网站没有原文。下单后我们将采用程序或人工为您竭诚获取高质量的原文,但由于OA文献来源多样且变更频繁,仍可能出现获取不到、文献不完整或与标题不符等情况,如果获取不到我们将提供退款服务。请知悉。

摘要

Most industrial production processes are performed in fed-batch operational mode. In contrast, the screenings for microbial production strains are run in batch mode which results in completely different physiological conditions than relevant for production. This may lead to wrong strain selections. Silicone elastomer discs containing glucose crystals were developed to realize fed-batch fermentation based on diffusion in shaken bioreactors. No other device for feeding was required. This “slow-release fed-batch technique” was tested on the metabolism of H. polymorpha, E. coli and G. oxydans in shake flasks. The OTR and RQ were monitored online with a RAMOS device. Biomass formation, synthesis of proteins like GFP or eYFP-IL-6, pH drift and metabolic dynamics of glucose, ethanol, acetic acid and other organic acids were measured offline. By application of the slow-release fed-batch technique in comparison to regular batch mode, overflow-metabolism of H. polymorpha and E. coli could be reduced, which led to an increase in biomass yield of up to 85% and 59%, respectively. Up to date, 23.4 g/L cell dry weight of H. polymorpha and 13.7 g/L of E. coli was achieved. The specific biomass yields of 0.38-0.47 are in the magnitude of those in laboratory fermentors equipped with a substrate feed-pump. The GFP expression by H. polymorpha RB11 pC10-GFP could be improved in Syn6-MES and YNB mineral media up to 35-fold and 420-fold, respectively. The synthesized maximum in fed-batch mode was 421 mg/L GFP. In contrast only up to 2.5 mg/L GFP was received in batch mode. The expression of eYFP-IL-6 by E. coli BL21 pLys pRSET eYFP-IL6 could be increased 4-fold in optimized Wilms-MOPS mineral medium using the slow-release fed-batch technique. Slow-release fed-batch cultures of G. oxydans DSM 2003 revealed a 2.6-fold increase of specific biomass yield in modified Silberbach-MES complex medium. A cell dry weight of 3.3 g/L was obtained in contrast to 1.6 g/L in batch mode. Due to glucose feeding a reduction of gluconic acid as well as 2- and 5-ketogluconic acid formation was monitored. A mass screening of 265 H. polymorpha RB11 pC10-FMD clones and 267 pC10-MOX clones was performed in Syn6-MES mineral medium in deep-well plates. A batch with glucose and one with glycerol were performed simultaneously in comparison to a slow-release fed-batch with glucose. One repetition screening was done under the same conditions. These diverse operational modes revealed great differences in strain selection and quality of specific GFP yield. The best strains for a fed-batch would be unlikely found in either batch mode. A dependence on the carbon source and the operational mode was found in relevance to the regulating promoter for gene expression. A fed-batch screening points out to be the most secure way to select the right strain for a fed-batch production process.
机译:大多数工业生产过程均以分批补料运行模式执行。相反,微生物生产菌株的筛选以分批模式进行,这导致与生产相关的生理条件完全不同。这可能会导致错误的应变选择。开发了包含葡萄糖晶体的有机硅弹性体圆盘,以基于在振动生物反应器中的扩散实现补料分批发酵。不需要其他进料装置。在摇瓶中对多形汉逊酵母,大肠埃希菌和氧化丁香假单胞菌的代谢测试了这种“缓释补料分批技术”。使用RAMOS设备在线监视OTR和RQ。离线测量了生物质形成,GFP或eYFP-IL-6等蛋白质的合成,pH漂移以及葡萄糖,乙醇,乙酸和其他有机酸的代谢动力学。与常规分批模式相比,通过应用缓释补料分批技术,可以减少多形汉逊酵母和大肠杆菌的溢流代谢,从而使生物量产量分别提高了85%和59%,分别。迄今为止,多形汉逊酵母的细胞干重为23.4 g / L,大肠杆菌为13.7 g / L。比生物量的产量为0.38-0.47,与配备底物给料泵的实验室发酵罐的产量相当。在Syn6-MES和YNB矿物培养基中,多形汉逊酵母RB11 pC10-GFP的GFP表达可以分别提高35倍和420倍。分批补料模式下合成的最大值为421 mg / L GFP。相比之下,分批模式仅接收高达2.5 mg / L的GFP。使用慢释补料分批技术,在优化的Wilms-MOPS矿物培养基中,大肠杆菌BL21 pLys pRSET pYSET eYFP-IL6的eYFP-IL-6的表达可以增加4倍。 G. oxydans DSM 2003的缓释补料分批培养表明,在改良的Silberbach-MES复合培养基中,特定生物量的产量提高了2.6倍。与分批模式下的1.6 g / L相比,电池的干重为3.3 g / L。由于葡萄糖进料,监测了葡糖酸的减少以及2-和5-酮葡糖酸的形成。在深孔板中的Syn6-MES矿物培养基中对265个多形汉逊酵母RB11 pC10-FMD克隆和267 pC10-MOX克隆进行了大规模筛选。与缓慢释放的葡萄糖补料分批比较,同时进行了葡萄糖分批和甘油分批补料。在相同条件下进行一次重复筛选。这些不同的操作模式显示出菌株选择和特定GFP产量的质量差异很大。在任一批处理模式下都不可能找到最佳的补料菌株。发现对碳源和操作模式的依赖性与基因表达的调节启动子有关。分批补料筛选是为分批补料生产过程选择合适菌株的最安全方法。

著录项

  • 作者

    Jeude Markus;

  • 作者单位
  • 年度 2007
  • 总页数
  • 原文格式 PDF
  • 正文语种 ger
  • 中图分类

相似文献

  • 外文文献
  • 中文文献
  • 专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号