葡萄糖和木糖双底物生物转化生产2,3-丁二醇和氢气的代谢计量分析

被引:7
作者
马成伟
孙亚琴
修志龙
机构
[1] 大连理工大学环境与生命学院
关键词
2,3-丁二醇; 氢; 葡萄糖; 木糖; 代谢计量分析;
D O I
暂无
中图分类号
TQ223.162 []; TQ116.2 [氢气];
学科分类号
0817 ;
摘要
以Klebsiella pneumoniae利用葡萄糖和木糖双底物生物转化生产2,3-丁二醇和氢气过程为研究对象,对其进行代谢计量分析。分析结果显示:2,3-丁二醇和氢气相对于底物葡萄糖和木糖的质量收率依赖于还原能力NADH2氧化磷酸化的分率(δ)。当δ=27时,即在总还原能力NADH2中有27mol NADH2被氧化磷酸化,剩余部分用来产生氢气,呼吸商为14时,2,3-丁二醇和氢气的最优质量收率分别为50%和0.8%;而当δ=1,即还原能力NADH2全部被氧化磷酸化、不产生氢气,呼吸商为4时,2,3-丁二醇的质量收率为37.5%;2,3-丁二醇和氢气的质量收率与底物中葡萄糖和木糖的比值无关。而氢气的摩尔收率与底物中葡萄糖和木糖的比值相关,当底物全部是葡萄糖或木糖时,其最优摩尔收率分别为71%和60%。该分析结果为葡萄糖和木糖双底物生物转化生产2,3-丁二醇过程的实验研究奠定了理论基础。
引用
收藏
页码:44 / 50
页数:7
相关论文
共 13 条
[1]  
Biological production of 2,3-butangeiol. Syu M J. Applied Microbiology and Biotechnology . 2001
[2]  
Effect of components of acid-hydrolysedhardwood on conversion of-Dxylose to 2,3-butanediol byKlebsiellapneumoniae. Frazer F R,McCaskey T A. Enzyme and Microbial Technology . 1991
[3]  
Current biological research in conversionof cellulosic carbohydrates into liquidfuels:how far havewe come. Flichinger MC. Biotechnology and Bioengineering . 1980
[4]  
Production of 2, 3-butanediol from D-xylose by Klebsiella oxytoca ATCC 8724. NB Jansen,GT Tsao. Biotechnology and Bioengineering . 1984
[5]  
Pathway analysis of glycerol fermentation by Klesiella pneumoniae:regulation of reducing equivalent balance and product formation. Zeng A-P. Enzyme and Microbial Technology . 1993
[6]  
Aspects of the metabolism of hydrogen production by Rhodobacter.sphaeroides. Koku H,Eroglu I,Gunduz U,Yucel M,Turker L. International Journal of Hydrogen Energy . 2002
[7]  
Production of 2,3-butane-diol from d-xylose byKlebsiella oxytocaATCC 8724. Norman B J,Jansen M C,Flickinger,et al. Biotechnology and Bioengineering . 1984
[8]  
Stoichiometric analysis and experimental investigation of glycerol bioconversion to 1, 3-propanediol by Klebsiella pneumoniae under microaerobic conditions. Chen X,,Xiu Z L,Wang J F et al. Enzyme and Microbial Technology . 2003
[9]  
Hydrogen production by bio- logical processes: A survey of literature. DAS D,,VEZIROGLU T N. Int J Hydro- gen Energy . 2001
[10]  
Use of respiratory quotient as a con-trol parameter for optimum oxygen supply and scale-up of 2,3-butane-diol production under microaerobic conditions. Zeng A P,Byun T G,Possten C. Biotechnology and Bioengineering .