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Two-stage pH Control Mode in Batch Fermentation of a Novel Bioflocculant from Corynebacterium Glutamicum 被引量:3
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作者 HENing WUXiao-jie DENGXu LUYing-hua LIQing-biao 《Chemical Research in Chinese Universities》 SCIE CAS CSCD 2004年第2期152-155,共4页
The effect of pH of the fermentation medium on cell growth and the production of a novel bioflocculant(named REA-11) by Corynebacterium glutamicum CCTCC M201005 were investigated. The maximum biomass(2.23 g/L) and fl... The effect of pH of the fermentation medium on cell growth and the production of a novel bioflocculant(named REA-11) by Corynebacterium glutamicum CCTCC M201005 were investigated. The maximum biomass(2.23 g/L) and flocculating activity(142.2 U/mL) were simultaneously obtained at the 14th hour when the pH value of the culture medium was maintained at 7.0 during the whole fermentation process. The production of REA-11 kept on a trend of increase till the later phase of fermentation process, which resulted in the ultimate flocculating activity of the culture broth to enhance to nearly 100 U/mL at pH 6.0. A two-stage pH control mode was adopted in REA-11 production in which the pH value of the culture medium was controlled at 7.0 during the first 14 h, then decreased to 6.0 that was maintained until the end of the fermentation process. With the two-stage pH control mode, the maximum flocculating activity reached 178.8 U/mL which was 30% higher than that obtained under the condition of pH 7.0 and the biomass enhanced about 15%. Compared with the fermentation process without pH control, REA-11 production and cell growth via the two-stage pH control mode increased 80% and 25%, respectively. 展开更多
关键词 corynebacterium glutamicum ph control bioflocculant
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两阶段pH控制和碳氮源协同补加促进谷氨酸棒杆菌高产L-谷氨酰胺
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作者 刘畅 陆丹丹 +2 位作者 浦军平 张春枝 陈明 《食品与发酵工业》 CSCD 北大核心 2024年第1期7-13,共7页
为提高谷氨酸棒杆菌发酵产L-谷氨酰胺产量、糖酸转化率、生产强度等技术指标,该文通过响应面法优化了摇瓶发酵培养基中葡萄糖、(NH_(4))_(2)SO_(4)和玉米浆含量,并利用50 L发酵罐进行分批发酵,构建了菌体生长、底物消耗和产物生成动力... 为提高谷氨酸棒杆菌发酵产L-谷氨酰胺产量、糖酸转化率、生产强度等技术指标,该文通过响应面法优化了摇瓶发酵培养基中葡萄糖、(NH_(4))_(2)SO_(4)和玉米浆含量,并利用50 L发酵罐进行分批发酵,构建了菌体生长、底物消耗和产物生成动力学模型,进而在50 L发酵罐中采用两阶段控制pH策略,并通过补加葡萄糖和(NH_(4))_(2)SO_(4),协同控制发酵液中碳氮源浓度,促进菌体高效合成L-谷氨酰胺。结果表明,优化后发酵培养基中葡萄糖、(NH_(4))_(2)SO_(4)和玉米浆含量分别为167、61、31 g/L,摇瓶发酵L-谷氨酰胺产量达到38.13 g/L,较优化前提高了34.12%;50 L发酵罐分批发酵80 h后L-谷氨酰胺产量达42.06 g/L,糖酸转化率达到25.85%,生产强度为0.53 g/(L·h);在50 L发酵罐中基于两阶段pH控制的碳氮源协同补加策略,显著促进了谷氨酸棒杆菌高产L-谷氨酰胺,发酵周期缩短至52 h,L-谷氨酰胺产量达68.01 g/L,糖酸转化率达33.93%,生产强度为1.31 g/(L·h)。该研究对促进L-谷氨酰胺的工业化生产具有重要参考价值。 展开更多
关键词 谷氨酸棒杆菌 L-谷氨酰胺 培养基优化 50 L发酵罐 两阶段ph控制 碳氮源协同补加
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