Bhargava Swapnil, Nandakumar M P, Roy Anindya, Wenger Kevin S, Marten Mark R
Department of Chemical and Biochemical Engineering, University of Maryland, Baltimore County, 1000 Hilltop Circle, Baltimore, Maryland 21250, USA.
Biotechnol Bioeng. 2003 Feb 5;81(3):341-7. doi: 10.1002/bit.10481.
The goal in this study was to determine if pulsed addition of substrate could be used to alter filamentous fungal morphology during fermentation, to result in reduced broth viscosity. In all experiments, an industrially relevant strain of Aspergillus oryzae was grown in 20-liter fermentors. As a control, cultures were fed limiting substrate (glucose) continuously. Tests were performed by altering the feeding strategy so that the same total amount of glucose was fed in repeated 300-s cycles, with the feed pump on for either 30 or 150 s during each cycle. Variables indicative of cellular metabolic activity (biomass concentration, oxygen uptake rate, base consumed for pH control) showed no significant difference between continuous and pulse-fed fermentations. In addition, there was no significant difference between total extracellular protein expression or the apparent distribution of these proteins. In contrast, fungal mycelia during the second half of pulse-fed fermentations were approximately half the size (average projected area) of fungi during fermentations with continuous addition of glucose. As a result, broth viscosity during the second half of pulse-fed fermentations was approximately half that during the second half of continuous fermentations. If these results prove to be applicable for other fungal strains and processes, then this method will represent a simple and inexpensive means to reduce viscosity during filamentous fungal fermentation.
本研究的目的是确定在发酵过程中脉冲添加底物是否可用于改变丝状真菌形态,从而降低发酵液粘度。在所有实验中,一株具有工业相关性的米曲霉在20升发酵罐中培养。作为对照,培养物持续供给限量底物(葡萄糖)。通过改变进料策略进行测试,使相同总量的葡萄糖以重复的300秒周期进料,每个周期进料泵开启30秒或150秒。指示细胞代谢活性的变量(生物量浓度、氧气摄取率、用于pH控制的碱消耗量)在连续进料发酵和脉冲进料发酵之间没有显著差异。此外,总细胞外蛋白表达或这些蛋白的表观分布也没有显著差异。相比之下,脉冲进料发酵后半段的真菌菌丝体大小(平均投影面积)约为连续添加葡萄糖发酵过程中真菌的一半。因此,脉冲进料发酵后半段的发酵液粘度约为连续发酵后半段的一半。如果这些结果被证明适用于其他真菌菌株和工艺,那么这种方法将代表一种简单且廉价的降低丝状真菌发酵过程中粘度的方法。