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中国农学通报 ›› 2013, Vol. 29 ›› Issue (18): 193-199.doi: 10.11924/j.issn.1000-6850.2012-3945

所属专题: 生物技术

• 食品 营养 检测 安全 • 上一篇    下一篇

地衣芽孢杆菌产β-甘露聚糖酶分批发酵动力学模型的建立

田雪 解鑫 周晓杭 葛菁萍   

  • 收稿日期:2012-12-05 修回日期:2013-02-22 出版日期:2013-06-25 发布日期:2013-06-25
  • 基金资助:
    国家自然科学基金;国家自然科学基金;黑龙江大学高层次人才(创新团队)支持计划

Research about Optimizated Fermentation Conditions of Production β-mannase from Bacillus Licheniformis HDYM - 04

ping jingge   

  • Received:2012-12-05 Revised:2013-02-22 Online:2013-06-25 Published:2013-06-25

摘要: 为研究其菌体生长、产物合成以及底物消耗情况,本文以分离自亚麻温水沤麻液的β-甘露聚糖酶高产菌株地衣芽孢杆菌(Bacillus licheniformis)HDYM-04为供试菌株。以初始魔芋粉加入量2 %、接种量6.7 %、初始pH值 8.0、培养温度37 ℃、搅拌速率300 r/min、通气量3 L/min、发酵周期30 h为基础发酵条件进行5L发酵罐发酵。并基于Logistic方程和Luedeking-Piret等方程建立了该菌株的菌体生长、产物生成、底物消耗三个分批发酵动力学模型,其相关系数分别为0.99021、0.98908、0.98812,均达到0.988以上,这些模型能真实描述菌体发酵过程中菌体生长、酶的合成以及底物消耗的情况。该试验为菌株HDYM-04的工业化应用奠定了理论基础并提供了实践指导,为小试数据的放大提供了重要参考。

关键词: 标准, 标准

Abstract: Abstract: In order to reseach on cell growthl, substrate depletion, production formation, Bacillus licheniformis strain HDYM-04 was isolated in flax retting and demonstrated a high production of β-mannanase. Use the fermentation conditions for fermentation as follows: the initial addition of konjac flour 2 % (w/v), inoculum 6.7 % (v/v) and the initial pH value of medium 8.0. The optimal process parameters including temperature, agitation speed and aeration rate optimized by orthogonal test were: temperature 37 ℃, agitation speed 300 r/min and aeration rate 3 L/min. Meanwhile, an optimal time course of fermentation cycle was 30 h. The establishment of batch fermentation kinetic models (cell growth kinetic model, substrate depletion kinetic model, production formation kinetic model) was based on Logistic and Luedeking-Piret equations. The correlation coefficients R2 of the three equations were 0.99021, 0.98908 and 0.98812, respectively, which indicated good correlation between experimental values and models. Therefore, the equations could be used to describe cell growth, enzyme synthesis and substrate consumption process of HDYM-04 during batch fermentation. Besides, the establishment of batch fermentation kinetic models (cell growth kinetic model, substrate depletion kinetic model, production formation kinetic model) could make theoretical foundation and provide practical instruction for the application of HDYM-04 in industry.