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Method of production of amino acids in a continuous manner by the use of a strain selected the adsorbed on a porous support and amino acids obtained by said other

机译:通过使用选择的吸附在多孔载体上的菌株以连续方式生产氨基酸的方法以及由所述另一种获得的氨基酸

摘要

Prodn. of aminoacids, pref. by a continuous process, comprises the use of at least one aminoacid producing bacterial strain in combination with a nutritative medium or appropriate fermentation contg. the necessary sources, such as assimilable carbon, organic nitrogen and mineral salts, is effected under aerobic conditions and is characterised in that the following stages are effected so as to increase the productivity and yield of the bacterial strain for producing aminoacids, with prodn. and regeneration of cofactors necessary for the reaction:- (a) the living cells of the bacterial strain are adsorbed on an appropriate porous support, placed in at least one reaction zone for fixing them onto the support, while conserving the living biomass; (b) the reaction zone is fed continuously with fermentation medium, while maintaining it at a suitable reaction temperature (pref. 15-60 deg.C. esp. 30-40 deg.C.), under suitable aeration to ensure the necessary oxygen supply. (c) fermented medium is continuously withdrawn after having passed through the reaction zone and (d) the withdrawn medium is extracted so as to recover the produced amino-acid. Continuous prodn. of aminoacids with improved productivity and yields is achieved. e.g. a typical batch process yields 40 g/l of aminoacid, after 80 hrs fermentation of a medium contg. 120 g/l of carbohydrates; known continuous processes yield 5 g/l of aminoacid, with 25 g/l of biomass after 30 hrs fermentation using 90 g/l of carbohydrate; whereas the present process yields 10 g/l of aminoacid, with a biomass of only 5 g/l and reaction time of 8 hrs using 90 g/l of carbohydrate. Examples for the prodn. of valine give the above results, other examples describe the prodn. of lysine and threonine.
机译:产品氨基酸,优选。通过连续方法,包括使用至少一种产生氨基酸的细菌菌株与营养培养基或适当的发酵续剂的组合。在有氧条件下产生必需的来源,例如可吸收的碳,有机氮和无机盐,其特征在于,进行以下步骤以提高生产氨基酸的细菌菌株的产率和收率。反应必需的辅因子的再生:-(a)将细菌菌株的活细胞吸附在适当的多孔载体上,该载体置于至少一个反应区中,以将它们固定在载体上,同时保留活生物质; (b)在适当通气的条件下,向反应区连续通入发酵培养基,同时将其保持在合适的反应温度(优选15-60℃,尤其是30-40℃)下,以确保必要的氧气供应。 (c)在经过反应区后连续取出发酵培养基,并且(d)提取取出的培养基以回收产生的氨基酸。连续产品实现了氨基酸产量的提高和产率的提高。例如典型的分批过程在浓缩的培养基发酵80小时后可产生40 g / l的氨基酸。 120克/升的碳水化合物;已知的连续过程使用90 g / l的碳水化合物发酵30小时后,产生5 g / l的氨基酸和25 g / l的生物量;而本发明方法产生的氨基酸量为10 g / l,生物量仅为5 g / l,使用90 g / l的碳水化合物的反应时间为8小时。产品示例缬氨酸的上述结果,其他例子描述。赖氨酸和苏氨酸。

著录项

  • 公开/公告号FR2509748B1

    专利类型

  • 公开/公告日1985-07-05

    原文格式PDF

  • 申请/专利权人 SANTERRE ORSAN PRODUITS ORGANIQU;

    申请/专利号FR19810013907

  • 发明设计人

    申请日1981-07-16

  • 分类号C12P13/08;C12R1/15;

  • 国家 FR

  • 入库时间 2022-08-22 07:56:08

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