重组褐藻胶裂解酶基因工程菌的高密度培养
High cell density culture of E.coli and high expression of recombinant alginate lyase
-
摘要: 在5L发酵罐中,利用分批补料培养技术高密度培养含表达褐藻胶裂解酶重组质粒的工程菌E.coliBL21,生产褐藻胶裂解酶。利用单因素实验对补料培养基中碳源浓度进行优化,利用单因素实验和单纯形优化法对诱导时间和IPTG浓度进行了优化,从而得到最适高密度发酵条件为:发酵培养基为葡萄糖10g/L,酵母提取物5g/L,蛋白胨20g/L;补料培养基为葡萄糖150g/L,蛋白胨20g/L,酵母提取物10g/L,4~10h的流加速率为100mL/h,10~16h的加速率设定为200mL/h;诱导时间为4.5h,IPTG终浓度为0.60mmol/L,发酵过程中溶解氧控制在30%~40%,pH控制在7.0~7.2。IPTG未诱导时,最终发酵液中菌液稀释200倍后,OD600达0.696,菌体浓度达65.38g/L;IPTG诱导后菌液稀释200倍后,OD600达0.457,菌体浓度达60.15g/L,是分批发酵的8.43倍;菌体进行超声波破碎后制备粗酶液,酶活力达26.37U/mL,是分批发酵的5.48倍。Abstract: In order to find the optimized condition to produce alginate lyase, using fed-batch culture technology, the engineered E.coli BL21 was cultured in 5L fermented at high density.The use of single-factor test to optimize the concentration of carbon source in the feed medium, single factor tests and simplex optimization method to optimize the induction time and IPTG concentration, to obtain optimal high-density fermentation conditions:fermentation medium glucose 10g/L, yeast extract 5g/L, peptone 20g/L.Feed medium was glucose 150g/L, peptone 20g/L, yeast extract 10g/L.The stream acceleration rate was set to 100mL/h form 4h to 10h.The stream acceleration rate was set to 200mL/h form 10h to16h.Induction time was at 4.5h, and the IPTG was final concentration to 0.60mmol/L.Dissolved oxygen in the fermentation process wad controlled in the 30% to 40%, and pH was controlled at 7.0~7.2.The results showed that in un-induced condition, the OD600 was 0.696 when final fermentation liquid were diluted 200 times.The engineered E.coli BL21 concentration was 65.38g/L.After induce with IPTG, the value of OD600 was 0.457 when fermentation liquid were diluted 200 times.The concentration of the engineered E.coli BL21 was 60.15g/L, which was 8.43 time compared with the value from the batch fermentation.Finally, the crude enzyme was extracted from the high density fermentation strain by ultrasonication.The enzyme activity was 26.37U/mL, which was up to 5.48 time compared with the batch fermentation.