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首页> 外文期刊>Bioresource Technology: Biomass, Bioenergy, Biowastes, Conversion Technologies, Biotransformations, Production Technologies >Enhanced ethanol fermentation in a pervaporation membrane bioreactor with the convenient permeate vapor recovery
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Enhanced ethanol fermentation in a pervaporation membrane bioreactor with the convenient permeate vapor recovery

机译:在渗透膜生物反应器中增强乙醇发酵,并具有方便的渗透蒸气回收功能

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摘要

A continuous and closed-circulating fermentation (CCCF) system with a pervaporation membrane bioreactor was built for ethanol fermentation without a refrigeration unit to condense the permeate vapor. Two runs of experiment with a feature of complete and continuous coupling of fermentation and pervaporation were carried out, lasting for 192 h and 264 h, respectively. The experimental measurement indicated that the enhanced fermentation could be achieved with additional advantages of convenient permeate recovery and energy saving of the process. During the second experiment, the average cell concentration, glucose consumption rate, ethanol productivity, ethanol yield and total ethanol amount produced reached 19.8 g L~(-1), 6.06 g L~(-1) h~(-1), 2.31 g L~(-1) h~(-1), 0.38, and 609.8 g L~(-1), respectively. During the continuous fermentation process, ethanol removal in situ promoted the cell second growth obviously, but the accumulation of the secondary metabolites in the broth became the main inhibitor against the cell growth and fermentation.
机译:构建了带有全蒸发膜生物反应器的连续和闭环发酵(CCCF)系统,用于乙醇发酵,而无需制冷单元来冷凝渗透蒸汽。进行了两个实验,其发酵和渗透蒸发完全连续地耦合,分别持续了192 h和264 h。实验测量表明,增强发酵可以通过便利的渗透物回收和节约过程的附加优点来实现。在第二个实验中,平均细胞浓度,葡萄糖消耗率,乙醇生产率,乙醇产量和产生的总乙醇量分别达到19.8 g L〜(-1),6.06 g L〜(-1)h〜(-1),2.31 g L〜(-1)h〜(-1),0.38和609.8 g L〜(-1)。在连续发酵过程中,原位去除乙醇明显促进了细胞的第二次生长,但肉汤中次生代谢产物的积累成为阻碍细胞生长和发酵的主要抑制剂。

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