Brandberg Tomas, Karimi Keikhosro, Taherzadeh Mohammad J, Franzén Carl Johan, Gustafsson Lena
Department of Chemical and Biological Engineering, Chalmers University of Technology, SE-412 96 Göteborg, Sweden.
Biotechnol Bioeng. 2007 Sep 1;98(1):80-90. doi: 10.1002/bit.21410.
Medium supplementation and process alternatives for fuel ethanol production from dilute acid lignocellulose hydrolysate were investigated. Dilute acid lignocellulose hydrolysate supplemented with enzymatically hydrolysed wheat flour could sustain continuous anaerobic cultivation of Saccharomyces cerevisiae ATCC 96581 if further supplemented with ammonium sulphate and biotin. This medium composition allowed for a hexose utilisation of 73% and an ethanol production of 36 mmol l(-1) h(-1) in chemostat cultivation at dilution rate 0.10 h(-1). Three different methods for cell retention were compared for improved fermentation of supplemented lignocellulose hydrolysate: cell recirculation by filtration, cell recirculation by sedimentation and cell immobilisation in calcium alginate. All three cell retention methods improved the hexose conversion and increased the volumetric ethanol production rate. Recirculation of 75% of the bioreactor outlet flow by filtration improved the hexose utilisation from 76% to 94%. Sedimentation turned out to be an efficient method for cell separation; the cell concentration in the reactor was 32 times higher than in the outflow after 60 h of substrate feeding. However, chemostat and continuous cell recirculation cultures became severely inhibited when the dilution rate was increased to 0.20 h(-1). In contrast, an immobilised system kept producing ethanol at a stable level also at dilution rate 0.30 h(-1).
研究了从稀酸木质纤维素水解液生产燃料乙醇的培养基补充和工艺替代方法。如果进一步补充硫酸铵和生物素,添加酶解小麦粉的稀酸木质纤维素水解液能够维持酿酒酵母ATCC 96581的连续厌氧培养。在稀释率为0.10 h(-1)的恒化器培养中,这种培养基组成允许己糖利用率达到73%,乙醇产量为36 mmol l(-1) h(-1)。比较了三种不同的细胞保留方法,以改善补充木质纤维素水解液的发酵:通过过滤进行细胞再循环、通过沉淀进行细胞再循环以及将细胞固定在海藻酸钙中。所有三种细胞保留方法都提高了己糖转化率并提高了乙醇体积生产率。通过过滤再循环75%的生物反应器流出物将己糖利用率从76%提高到了94%。沉淀被证明是一种有效的细胞分离方法;在底物进料60小时后,反应器中的细胞浓度比流出物中的细胞浓度高32倍。然而,当稀释率提高到0.20 h(-1)时,恒化器和连续细胞再循环培养受到严重抑制。相比之下,固定化系统在稀释率为0.30 h(-1)时也能保持稳定的乙醇产量。