National Energy R&D Center for Biorefinery, Beijing University of Chemical Technology, Beijing 100029, PR China; Beijing Tiantian Biological Products Corporation Limited, Beijing 100176, PR China.
National Energy R&D Center for Biorefinery, Beijing University of Chemical Technology, Beijing 100029, PR China.
Bioresour Technol. 2016 Apr;205:82-9. doi: 10.1016/j.biortech.2016.01.034. Epub 2016 Jan 21.
In order to make full use of the fresh corn stalk, the sugar containing juice was used as the sole substrate for acetone-butanol-ethanol production without any nutrients supplement, and the bagasse after squeezing the juice was used as the immobilized carrier. A total 21.34g/L of ABE was produced in batch cells immobilization system with ABE yield of 0.35g/g. A continuous fermentation containing three stages with immobilized cells was conducted and the effect of dilution rate on fermentation was investigated. As a result, the productivity and ABE solvents concentration reached 0.80g/Lh and 19.93g/L, respectively, when the dilution rate in each stage was 0.12/h (corresponding to a dilution rate of 0.04/h in the whole system). And the long-term operation indicated the continuous multiple stages ABE fermentation process had good stability and showed the great potential in future industrial applications.
为了充分利用新鲜的玉米秸秆,将含有糖分的汁液用作丙酮-丁醇-乙醇生产的唯一底物,无需任何营养物质补充,并且榨汁后的甘蔗渣用作固定化载体。在分批细胞固定化系统中,共生产了 21.34g/L 的 ABE,ABE 得率为 0.35g/g。进行了含有三个阶段的连续发酵,并研究了稀释率对发酵的影响。结果,当每个阶段的稀释率分别为 0.12/h(相当于整个系统中的稀释率为 0.04/h)时,产物得率和 ABE 溶剂浓度分别达到 0.80g/Lh 和 19.93g/L。长期运行表明,连续多级 ABE 发酵过程具有良好的稳定性,在未来的工业应用中具有很大的潜力。