Department of Agricultural Sciences, Biotechnology and Food Science, Cyprus University of Technology, Lemesos CY 3603, P.O. Box 50329, Cyprus.
Bioresour Technol. 2012 Jun;114:492-8. doi: 10.1016/j.biortech.2012.03.010. Epub 2012 Mar 10.
Saccharomyces cerevisiae was immobilized on γ-alumina pellets and used for repeated batch fermentations in glucose medium (16.5 g/100 mL) at various temperatures and pressures. An increase in pressure from 3 to 7 atm and a decrease in temperature from 30 to 20 °C reduced the ethanol productivity by about 50% and 70%, respectively. Increasing concentrations of volatile by-products were observed at lower fermentation temperatures, while the pressure influence on the concentrations of these by-products was proved to be more complex. Mathematical expressions were established to allow the calculation of the fermentation rate at various pressures and sugar concentrations when the corresponding rate at atmospheric pressure is known. The study showed that the height of bioreactors has to be limited to 19.5 m due to hydrostatic pressure shock at higher fill levels.
酿酒酵母被固定在γ-氧化铝小球上,并在不同温度和压力下的葡萄糖培养基(16.5 g/100 mL)中进行分批重复发酵。压力从 3 大气压增加到 7 大气压,温度从 30°C 降低到 20°C,乙醇的生产率分别降低了约 50%和 70%。在较低的发酵温度下,观察到挥发性副产物的浓度增加,而压力对这些副产物浓度的影响则更为复杂。建立了数学表达式,以便在已知大气压下相应的发酵速率时,计算不同压力和糖浓度下的发酵速率。研究表明,由于较高填充水平下的静压冲击,生物反应器的高度必须限制在 19.5 m 以内。