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作 者:朱婧[1] 吴昊[1] 任心怡[1] 张敏[1] 马江锋[1] 姜岷[1]
机构地区:[1]南京工业大学生物与制药工程学院材料化学工程国家重点实验室,江苏南京211816
出 处:《化工进展》2015年第12期4333-4337,共5页Chemical Industry and Engineering Progress
基 金:江苏高校优势学科建设工程项目(PAPD);新世纪优秀人才支持计划(NCET-12-0732)项目
摘 要:为了降低生物法制备甘露醇的成本,以假肠膜明串珠菌Leuconostoc pseudomesenteroides G123为研究对象,对培养基中的氮源、葡萄糖与果糖比例和p H调控过程进行了优化,提高了果糖转化率和甘露醇产量。5L发酵罐中结果显示:采用2g/L的酵母粉作为单一氮源,葡萄糖和果糖的比例为0.35∶1,初始p H值7.5,发酵过程中保持p H值不低于4.5,甘露醇产量可达57.24g/L,甘露醇对果糖的转化率为83.2%。该过程副产D-乳酸20.32g/L,其光学纯度达99.9%,具有回收价值,甘露醇与D-乳酸对糖总转化率为89.38%,有助于降低生物法制备甘露醇的成本。A new mutant strain Leuconostoc pseudomesenteroides G123 was investigated in this study. The nitrogen source,the ratio of glucose and fructose and the p H control strategy were optimized to reduce the cost of mannitol production. Batch fermentations were operated in a 5L fermentor.The results showed that 57.24g/L mannitol was produced with the mannitol yield of 83.2% when 2g/L yeast extract was chosen as the single nitrogen source,the ratio of fructose toglucose was 0.35∶1,and the initial p H was controlled at 7.5 and kept constant at 4.5 in the later phase. Besides,20.32g/L D-lactic acid with optical purity of 99.9% was also produced which suggested it could be recovered as a by-product. The yield of mannitol and lactic acid to the total sugar was 89.38%. As a result,the cost was reduced efficiently.
分 类 号:TQ923[轻工技术与工程—发酵工程]
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