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多粘类芽孢杆菌同步糖化发酵玉米粉生产(R,R)-2,3-丁二醇
引用本文:李亿,李检秀,刘海余,黄艳燕,陆琦,谢能中,黄日波. 多粘类芽孢杆菌同步糖化发酵玉米粉生产(R,R)-2,3-丁二醇[J]. 广西科学, 2016, 23(1): 41-46. DOI: 10.3969/j.issn.1005-9164.2016.01.008
作者姓名:李亿  李检秀  刘海余  黄艳燕  陆琦  谢能中  黄日波
作者单位:1. 广西大学生命科学与技术学院,广西南宁530005;广西科学院,非粮生物质酶解国家重点实验室,国家非粮生物质能源工程技术研究中心,广西生物炼制重点实验室,广西生物质产业化工程院,广西南宁 530007;2. 广西大学生命科学与技术学院,广西南宁,530005;3. 广西科学院,非粮生物质酶解国家重点实验室,国家非粮生物质能源工程技术研究中心,广西生物炼制重点实验室,广西生物质产业化工程院,广西南宁 530007
基金项目:国家自然科学基金项目(31400079;31160023),中科院微生物生理与代谢工程重点实验室开放课题(KLIM-201304),广西科学研究与技术开发计划项目(桂科合14125008-2-22)
摘    要:【目的】对多粘类芽孢杆菌Paenibacillus polymyxa的玉米粉同步糖化发酵工艺进行优化,以获得低成本、高效的(R,R)-2,3-丁二醇生产技术。【方法】研究玉米粉浓度、氮源种类和氮源浓度对菌体生长、耗糖能力以及(R,R)-2,3-丁二醇产量、产率、得率和转化率的影响,并在此基础上进一步考察培养基中其它成分对(R,R)-2,3-丁二醇发酵的影响。【结果】优化后的培养基组分为玉米干粉140g/L,酵母粉30g/L,Na_2HPO_4 3g/L,KH_2PO_43g/L,(NH_4)2SO_42g/L,MgSO_40.8g/L,微量元素溶液2mL/L。使用优化后的培养基进行同步糖化发酵,发酵50h后(R,R)-2,3-丁二醇产量达到56.28g/L(光学纯度为98.3%),对葡萄糖的得率为0.44g/g,产率为1.13g/(L·h)。【结论】(R,R)-2,3-丁二醇生产技术低价高效,可为其工业化生产提供参考。

关 键 词:(R,R)-2,3-丁二醇  多粘类芽孢杆菌  同步糖化  发酵工艺  低价碳源
收稿时间:2015-11-13
修稿时间:2016-01-26

Simultaneous Sccharification and(R,R)-2,3-butanediol Fermentation from Corn Flour by Paenibacillus polymyxa
LI Yi,LI Jianxiu,LIU Haiyu,HUANG Yanyan,LU Qi,XIE Nengzhong and HUANG Ribo. Simultaneous Sccharification and(R,R)-2,3-butanediol Fermentation from Corn Flour by Paenibacillus polymyxa[J]. Guangxi Sciences, 2016, 23(1): 41-46. DOI: 10.3969/j.issn.1005-9164.2016.01.008
Authors:LI Yi  LI Jianxiu  LIU Haiyu  HUANG Yanyan  LU Qi  XIE Nengzhong  HUANG Ribo
Affiliation:College of Life Science and Technology, Guangxi University, Nanning, Guangxi, 530005, China;State Key Laboratory of Non-food Biomass and Enzyme Technology, National Engineering Research Center for Non-food Biorefinery, Guangxi Key Laboratory of Biorefinery, Guangxi Biomass Industrialization Engineering Institute, Guangxi Academy of Sciences, Nanning, Guangxi, 530007, China,College of Life Science and Technology, Guangxi University, Nanning, Guangxi, 530005, China;State Key Laboratory of Non-food Biomass and Enzyme Technology, National Engineering Research Center for Non-food Biorefinery, Guangxi Key Laboratory of Biorefinery, Guangxi Biomass Industrialization Engineering Institute, Guangxi Academy of Sciences, Nanning, Guangxi, 530007, China,College of Life Science and Technology, Guangxi University, Nanning, Guangxi, 530005, China,State Key Laboratory of Non-food Biomass and Enzyme Technology, National Engineering Research Center for Non-food Biorefinery, Guangxi Key Laboratory of Biorefinery, Guangxi Biomass Industrialization Engineering Institute, Guangxi Academy of Sciences, Nanning, Guangxi, 530007, China,State Key Laboratory of Non-food Biomass and Enzyme Technology, National Engineering Research Center for Non-food Biorefinery, Guangxi Key Laboratory of Biorefinery, Guangxi Biomass Industrialization Engineering Institute, Guangxi Academy of Sciences, Nanning, Guangxi, 530007, China,State Key Laboratory of Non-food Biomass and Enzyme Technology, National Engineering Research Center for Non-food Biorefinery, Guangxi Key Laboratory of Biorefinery, Guangxi Biomass Industrialization Engineering Institute, Guangxi Academy of Sciences, Nanning, Guangxi, 530007, China and College of Life Science and Technology, Guangxi University, Nanning, Guangxi, 530005, China;State Key Laboratory of Non-food Biomass and Enzyme Technology, National Engineering Research Center for Non-food Biorefinery, Guangxi Key Laboratory of Biorefinery, Guangxi Biomass Industrialization Engineering Institute, Guangxi Academy of Sciences, Nanning, Guangxi, 530007, China
Abstract:[Objectives] In this study, corn flour simultaneous saccharification and fermentationprocess was optimized to achieve a low-cost and efficient (R, R)-2, 3-butanediol production technology.[Methods] The effects of different types and concentrations of nitrogen, and different concentrations of corn flour on cell growth, consumption of sugar, (R, R)-2, 3-butanediol production, productivity, yield and conversion rate were investigated based on corn flour simultaneous saccharification and fermentation.Furthermore, the effects of other components in the medium on (R, R)-2, 3-butanediol fermentation were observed.[Results] The optimized composi-tion of culture medium was as follows:140g/L dried corn flour, 30g/L yeast extract, 3g/L Na2HPO4, 3g/L KH2PO4, 2g/L (NH4)2SO4, 0.8g/L MgSO4 and 2mL/L trace element solution.Under abovementioned conditions, up to 56.28g/L (R, R)-2, 3-butanediol (optical purity >98.3%)could be achieved within 50 hwith the yield on glucose of 0.44g/g and the conversion rate of 1.13g/(L·h).This is the highest production of (R, R)-2, 3-butanediol titer so far reported from low-cost carbon source.[Conclusion] This study develops a technology utilizing low-cost carbon to produce (R, R)-2, 3-butanediol efficiently, which provides meaningful guidance for its future industrial production. More
Keywords:(R,R)-2,3-butanediol  Paenibacillus polymyxa  simultaneous saccharification  fermentation process  low-cost carbon source
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