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用于连续乳酸发酵的厌氧膜生物反应器

Anaerobic Membrane Bioreactor for Continuous Lactic Acid Fermentation.

作者信息

Fan Rong, Ebrahimi Mehrdad, Czermak Peter

机构信息

Institute of Bioprocess Engineering and Membrane Technology, University of Applied Sciences Mittelhessen, Giessen 35390, Germany.

Department of Chemical Engineering, Kansas State University, Manhattan, KS 66506, USA.

出版信息

Membranes (Basel). 2017 May 3;7(2):26. doi: 10.3390/membranes7020026.

Abstract

Membrane bioreactor systems can enhance anaerobic lactic acid fermentation by reducing product inhibition, thus increasing productivity. In batch fermentations, the bioconversion of glucose is strongly inhibited in the presence of more than 100 g·L lactic acid and is only possible when the product is simultaneously removed, which can be achieved by ceramic membrane filtration. The crossflow velocity is a more important determinant of flux than the transmembrane pressure. Therefore, to stabilize the performance of the membrane bioreactor system during continuous fermentation, the crossflow velocity was controlled by varying the biomass concentration, which was monitored in real-time using an optical sensor. Continuous fermentation under these conditions, thus, achieved a stable productivity of ~8 g·L·h and the concentration of lactic acid was maintained at ~40 g·L at a dilution rate of 0.2 h. No residual sugar was detected in the steady state with a feed concentration of 50 g·L.

摘要

膜生物反应器系统可通过减少产物抑制来增强厌氧乳酸发酵,从而提高生产率。在分批发酵中,当乳酸浓度超过100 g·L时,葡萄糖的生物转化会受到强烈抑制,只有在同时去除产物的情况下才有可能实现,这可以通过陶瓷膜过滤来实现。错流速度比跨膜压力对通量的影响更重要。因此,为了在连续发酵过程中稳定膜生物反应器系统的性能,通过改变生物质浓度来控制错流速度,生物质浓度使用光学传感器进行实时监测。在这些条件下进行连续发酵,从而实现了约8 g·L·h的稳定生产率,在稀释率为0.2 h时,乳酸浓度保持在约40 g·L。在进料浓度为50 g·L的稳态下未检测到残留糖。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/87a8/5489860/2221b3b1f19e/membranes-07-00026-g001.jpg

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