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作 者:彭志坚[1,2] 房峻[1,2] 李江华[1,2] 堵国成[1,2] 陈坚[1,2] 宁健飞 蔡立明
机构地区:[1]江南大学工业生物技术教育部重点实验室 [2]江南大学生物工程学院,无锡214122 [3]无锡晶海氨基酸有限公司
出 处:《工业微生物》2009年第3期11-16,共6页Industrial Microbiology
基 金:国家高技术研究发展计划(863)项目资助(No.2007AA02Z229)。
摘 要:研究了溶氧对Brevibacterium lactofermentation分批发酵生产L-异亮氨酸(Ile)的影响,提出了前10h恒700r/min以维持溶氧在35%以上,10h后调至600r/min以维持溶氧在15%~20%的两阶段供氧控制模式。与对照相比,获得了较高的产率(0.094g/g)和糖耗速度(4.76g/L·h),在较短时间内(52h)获得较高的Ile产量(23.3g/L),比结果最好的单一搅拌转速(600r/min)提高11.6%。生产强度(0.448g/L·h)比恒定搅拌转速(500、600、700、800r/min)控制下的过程分别提高了83.6%、28.7%、44.9%、35.7%。最后采用代谢通量分析对该结果产生的原因进行了定量解释。The effect of dissolved oxygen (DO) on L-isoleucine production by Brevibacterium lactofermentation was investigated in batch fermentation process. A two-stage DO control strategy was developed, in which the agitation speed was controlled at 700 r/min during in the first 10 h to achieve a DO level up to 35%, and then switched to 600 r/min after 10 h to maintain a DO level at 15% --20 %. A relative high yield (0. 094 g/g) and glucose consumption rate (4.76 g/L·h) were obtained. The high isoleueine production (23.3 g/L) was achieved in a relative short period (52 h), and it was increased by 11.6o,6 compared to the highest value ofby using single agitation speed (600 r/min). According to the results in constant agitation speed (500, 600, 700, 800 r/min), the productivity (0. 448 g/L·h) was increased by 83.6 %, 28.7%, 44.9 %, and 35.7 %, respectively. Finally, the reason for the increase of isoleucine production with the proposed two-stage DO control strategy was quantitatively described in detail by analysis of metabolic flux distribution in metabolic network of isoleucine production by Brevibacterium lactofermentation.
关 键 词:异亮氨酸 BREVIBACTERIUM lactofermentation 分批发酵 溶氧控制 代谢通量
分 类 号:TQ922.9[轻工技术与工程—发酵工程] TQ929
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