Department of Fermentation Technology, Institute of Food Science and Biotechnology, Hohenheim Universität, Garbenstrasse 23, 70599 Stuttgart, Germany.
Bioresour Technol. 2012 Nov;123:221-9. doi: 10.1016/j.biortech.2012.07.032. Epub 2012 Jul 20.
A gas lift-system with inserts (so-called Blenke cascade system) for continuous bio-ethanol fermentation was constructed. Gas introduced at the bottom of the column created toroidal vortices in the fluid cells between inserts, enhancing mixing and improving residence time behavior without stirring equipment being necessary. The parameters mash type, start-up strategy, yeast-recycle model and yeast separation were studied concerning the efficiency of the ethanol production. The best results obtained were for a filtered mash, a double saccharification principle (DSP), a batch start-up strategy, an activation-recycle model and a lamella settler connected in series with a small conventional gravitational settler for yeast cells separation. Using this system, the fermentation residence time was τ=4-5.5h, depending on substrate type. Eighty five percent of the yeast cells could be separated. High volumetric ethanol productivity (Q(p)=20.43g/Lh) and yield E(y)=98% were achieved. Continuous fermentation, yeast recycling and sedimentation were contamination-free processes.
构建了一种带有插入件(所谓的 Blenke 级联系统)的气体升力系统,用于连续的生物乙醇发酵。气体从柱体底部引入,在插入件之间的流体单元中形成环形涡旋,增强了混合效果,改善了停留时间行为,而无需搅拌设备。研究了醪液类型、启动策略、酵母循环模型和酵母分离等参数,以考察乙醇生产的效率。最佳结果是采用过滤醪液、双糖化原理(DSP)、分批启动策略、激活循环模型和与小型传统重力沉降器串联的板式沉降器来分离酵母细胞。使用该系统,发酵停留时间τ=4-5.5h,取决于底物类型。可分离 85%的酵母细胞。实现了高的乙醇体积产率(Q(p)=20.43g/Lh)和产率 E(y)=98%。连续发酵、酵母回收和沉降是无污染的过程。