三段式谷氨酸棒杆菌发酵生产生物絮凝剂的过程及动力学模拟(英文)

Fermentation of bioflocculant with Corynebacterium glutamicum was studied by way of kinetic modeling. Lorentzian modified Logistic model, time-corrected Luedeking–Piret and Luedeking–Piret type models were pro-posed and applied to describe the cell growth, bioflocculant synthesis and consumption of substrates, with the correlation of initial biomass concentration and initial glucose concentration, respectively. The results showed that these models could well characterize the batch culture process of C. glutamicum at various initial glucose con-centrations from 10.0 to 17.5 g·L?1. The initial biomass concentration could shorten the lag time of cel growth, while the maximum biomass concentration was achieved only at the optimal initial glucose concentration of 16.22 g·L?1. A novel three-stage fed-batch strategy for bioflocculant production was developed based on the model prediction, in which the lag phase, quick biomass growth and bioflocculant production stages were sequentially proceeded with the adjustment of glucose concentration and dissolved oxygen. Biomass of 2.23 g·L?1 was obtained and bioflocculant concentration was enhanced to 176.32 mg·L?1, 18.62% and 403.63%higher than those in the batch process, respectively, indicating an efficient fed-batch culture strategy for bioflocculant production.     

谷氨酸棒杆菌合成生物絮凝剂分批发酵过程的动力学模拟

对谷氨酸棒杆菌生产生物絮凝剂的分批发酵过程进行了动力学研究。以Logistic方程来描述菌体生长过程,并对Gaden生长相关模型进行了修正,加入时间修正因子,建立了产物生成动力学模型,同时还提出了关于葡萄糖和尿素的两个非线性基质消耗动力学模型。利用软件Origin 8.0对实验数据进行拟合,结果显示各模型均能较好地描述谷氨酸棒杆菌合成生物絮凝剂的分批发酵过程。