Taylor F, Kurantz M J, Goldberg N, Craig J C
Agricultural Research Service, Eastern Regional Research Center, Philadelphia, Pennsylvania 19118, USA.
Biotechnol Prog. 1995 Nov-Dec;11(6):693-8. doi: 10.1021/bp00036a014.
Recycling the contents of a continuous fermentor through a stripping column is proposed as a means of reducing product inhibition and lowering the cost of fuel ethanol production. A 2-L fermentor and 10-cm packed column were continuously operated for 150 days without contamination. Some fouling of the packing with attached yeast cells was observed which partially blocked the column. Cell yield was lower than in a simple continuous fermentor. Complete conversion of 200 g/L glucose feed and 90% conversion of 600 g/L glucose feed were achieved. Data were analyzed by computerized process simulation. Cost analysis indicated that, with heat recovery to reduce heating and cooling costs, the continuous fermentor/stripper is possibly a lower-cost alternative to conventional fermentation and distillation.
有人提出通过汽提塔循环连续发酵罐的内容物,以此作为减少产物抑制并降低燃料乙醇生产成本的一种方法。一个2升的发酵罐和一个10厘米的填充柱连续运行了150天且未受污染。观察到填料上附着有酵母细胞,出现了一些结垢现象,部分堵塞了柱子。细胞产量低于简单的连续发酵罐。实现了200克/升葡萄糖进料的完全转化以及600克/升葡萄糖进料90%的转化。通过计算机化过程模拟对数据进行了分析。成本分析表明,通过热量回收以降低加热和冷却成本,连续发酵罐/汽提塔可能是一种比传统发酵和蒸馏成本更低的替代方案。