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机构地区:[1]华东理工大学生物反应器工程国家重点实验室,上海200237
出 处:《过程工程学报》2014年第1期133-138,共6页The Chinese Journal of Process Engineering
基 金:国家高技术研究发展计划(863)基金资助项目(编号:2012AA022104)
摘 要:对表达了高效醛脱氢酶的重组肺炎克雷伯氏菌以甘油为底物生产3.羟基丙酸和1,3-丙二醇的过程进行优化,将发酵过程中补料阶段甘油浓度分别控制为0-10,10-20,20-30g/L,并分3次间歇性补加甘油.结果表明,发酵过程中补料阶段控制甘油浓度在20~30g/L,发酵26h得到47.20g/L3-羟基丙酸和43.90g/L1,3一丙二醇;而间歇性补加甘油产物得率最高,发酵26h时3.羟基丙酸和1,3-丙二醇相对甘油的得率分别为0.35和0.38mol/m01.3-羟基丙酸和1,3-丙二醇联产可实现辅因子烟酰胺腺嘌呤二核苷酸的再生平衡,从而提高碳回收率.The production of 3-hydroxypropionic acid (3-HP) and 1,3-propanediol (1,3-PDO) by recombinant Klebsiella pneumoniae over-expressed aldehyde dehydrogenase was optimized with glycerol as substrate. During the feeding stage of fermentation, glycerol concentration was controlled differently at 0-10, 10-20, 20-30 g/L and intermittent addition of glycerol for three times. The results showed that the process controlling of glycerol concentration at 20-30 g/L resulted in the highest titer, 47.20 g/L of 3-HP and 43.90 g/L of 1,3-PDO were obtained in 26 h. The intermittent addition of glycerol led to the highest yield of 3-HP and 1,3-PDO, 0.35 and 0.38 mol/mol, respectively. The co-production of 3-HP and 1,3-PDO could achieve cofactor regeneration of NAD+ and NADH balance, which enhanced the recovery of carbon.
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