...
首页> 外文期刊>Bioresource Technology: Biomass, Bioenergy, Biowastes, Conversion Technologies, Biotransformations, Production Technologies >Oxygen uptake rate optimization with nitrogen regulation for erythromycin production and scale-up from 50 L to 372 m~3 scale
【24h】

Oxygen uptake rate optimization with nitrogen regulation for erythromycin production and scale-up from 50 L to 372 m~3 scale

机译:通过氮调节来优化红霉素生产的吸氧率,并从50 L扩大到372 m〜3规模

获取原文
获取原文并翻译 | 示例
           

摘要

Effects of different nitrogen sources on the erythromycin production were investigated in 50 l fermenter with multi-parameter monitoring system firstly. With the increase of soybean flour concentration from 27 g/l to 37 g/l to the culture medium, the erythromycin production had no obvious increase. Whereas adding corn steep liquor 15 g/l in the medium was beneficial for the production of erythromycin, the maximum erythromycin production was 22.2% higher than that of the control. It was found that corn steep liquor can regulate and enhance the oxygen uptake rate (OUR) which characterizes the activity of the microbial metabolism by inter-scale observation and data association. Both Intracellular and extracellular organic acids of central metabolism were analyzed, and it was found that the whole levels of lactic acid, pyruvic acid, citric acid, and propionic acid were higher than those of control before 64th h. The consumption amount of amino acids, which could be transformed into the precursors for erythromycin synthesis (i.e. threonine, serine, alanine, glycine and phenylalanine), were elevated compared with the control in erythromycin biosynthesis phase. The results indicated that corn steep liquor can regulate OUR to certain level in the early phase of fermentation, and enhance the metabolic flux of erythromycin biosynthesis. Erythromycin production was successfully scaled up from a laboratory scale (50 l fermenter) to an industrial scale (132 m~3 and 372 m~3) using OUR as the scale-up parameter. Erythromycin production on industrial scale was similar to that at laboratory scale.
机译:首先利用多参数监测系统研究了50升发酵罐中不同氮源对红霉素生产的影响。随着培养基中大豆粉浓度从27 g / l增加到37 g / l,红霉素的产量没有明显增加。尽管在培养基中添加15 g / l的玉米浆对红霉素的生产是有利的,但最大的红霉素产量比对照组高22.2%。已发现玉米浸泡液可以通过尺度间的观察和数据关联来调节和提高吸氧率(OUR),这是微生物代谢活性的特征。分析了中心代谢的细胞内和细胞外有机酸,发现乳酸,丙酮酸,柠檬酸和丙酸的总体水平在第64 h之前高于对照组。与红霉素生物合成阶段的对照相比,可以转化为红霉素合成前体(即苏氨酸,丝氨酸,丙氨酸,甘氨酸和苯丙氨酸)的氨基酸消耗量增加了。结果表明,玉米浸液可以在发酵初期将OUR调节至一定水平,并提高红霉素的生物合成代谢通量。使用OUR作为放大参数,成功地将红霉素的生产规模从实验室规模(50升发酵罐)扩大到了工业规模(132 m〜3和372 m〜3)。工业规模的红霉素生产与实验室规模的生产相似。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

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