首页> 外国专利> MEMBRANE-BASED PROCESS FOR THE RECOVERY OF LACTIC ACID BY FERMENTATION OF CARBOHYDRATE SUBSTRATES CONTAINING FERMENTABLE SUGARS

MEMBRANE-BASED PROCESS FOR THE RECOVERY OF LACTIC ACID BY FERMENTATION OF CARBOHYDRATE SUBSTRATES CONTAINING FERMENTABLE SUGARS

机译:发酵含糖碳水化合物的发酵过程中基于膜的乳酸回收方法

摘要

MEMBRANE-BASED PROCESS FOR THE RECOVERY OF LACTIC ACID BY FERMENTATION OF CARBOHYDRATE SUBSTRATES CONTAINING FERMENTABLE SUGARS OF THE DISCLSOURE A substantially continuous membrane separation process has been discovered in which the known benefits of a cellrecycle fermentor are unexpectedly enhanced because pH is controlled from 4.0 to 5.5 with a nitrogen-containing base, most preferably ammonium hydroxide. The ammonium lactate formed is not precipitated. This allows continuous removal of lactic acid so as to maintain a concentration of lactic acid about 12%, preferably about 6% by wt in the broth, optionally supplemented with thin stillage or steep water, and optionally buffered with protease. When combined with recycle of UF retentate, operating this cell-recycle fermentor allows the build-up of a cell population in the range from above 5 x 109 CFU/ml to 5 x 1010 CFU/ml, which population is much denser than one which can be produced with the specified pH control in a batch fermentor, after self-termination of the fermentation. This super-dense population of cells, in turn, not only accelerates production of lactic acid but also minimizes contamination by foreign cells; and since the UF retentate is recycled, a relatively large portion of the broth in the fermentor may be withdrawn as a fermentor effluent stream, sufficient to produce a specified high fluid velocity when the effluent stream is flowed over UF membranes used in the UF modules. The high fluid velocity, preferably from 5-10 m/sec, at. relatively flow pressure less than 1140 kPa (150 psig), produces a scrubbing action over the membrane surfaces which are therefore not fouled over long periods of operation. In a batch fermentation with pH control, when the fermentation is self-terminated the total lactic acid present is about 10% by wt (measured by HPLC), though free always 4%, and the live cell population is lower than 5 x 109 CFU/ml because many cells die as pH drops.
机译:膜发酵过程中含有可发酵糖的碳水化合物回收乳酸的方法,发现一种基本上连续的膜分离方法,由于pH值控制在4.0至5.5之间,因此细胞发酵罐的已知优势得到了意外的提高。用含氮的碱,最优选氢氧化铵。形成的乳酸铵没有沉淀。这允许连续除去乳酸,以保持肉汤中乳酸的浓度为约12重量%,优选约6重量%,任选地补充稀釜馏物或浸泡水,并任选地用蛋白酶缓冲。当与UF截留物的回收结合使用时,操作此细胞回收发酵罐可建立5×109 CFU / ml以上至5×1010 CFU / ml以上的细胞群,该细胞群比一个细胞群致密得多。发酵自终止后,可以在分批发酵罐中使用指定的pH控制来生产。反过来,这种超高密度的细胞群不仅可以加速乳酸的产生,还可以最大限度地减少外来细胞的污染。并且由于UF滞留物被回收,因此可以将发酵罐中相对较高的发酵液作为发酵罐废水排出,当废水流过UF模块中使用的UF膜时足以产生特定的高流速。较高的流体速度,优选为5-10 m / sec。相对小于1140 kPa(150 psig)的流动压力会在膜表面产生擦洗作用,因此在长期运行时不会结垢。在具有pH控制的分批发酵中,当发酵自行终止时,存在的乳酸总量约为10 wt%(通过HPLC测定),尽管游离总是<4%,并且活细胞总数低于5 x 109 CFU / ml,因为许多细胞会随着pH下降而死亡。

著录项

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

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