摘要
研究了毕赤酵母高密度发酵组成型表达α-葡聚糖酶,从6.8 L发酵罐逐级放大至5000 L发酵罐的放大工艺。采用恒定p H和控制甘油残留浓度和溶解氧相结合的调控策略,进行了多批次的发酵试验。结果表明:三磷酸甘油醛脱氢酶启动子驱动的α-葡聚糖酶的生成具有生长偶联特征,集中在对数生长期和稳定期。6.8 L发酵罐中上清酶活达1253 U/m L,中试放大至50 L发酵罐中产酶最高达1300 U/m L,500 L发酵罐中酶活为740 U/m L。5000 L规模发酵罐中产酶达到589 U/m L。建立了以甘油作为碳源,发酵调控简单的工艺,避免了使用甲醇带来的安全问题,适合放大生产。
The high density fermentation of dextranase in the constitutive Pichia pastoris expression system scaled up from 6.8 to 5000 L in series was studied. By controlling residual concentration of glycerol and dissolved oxygen combined with p H-stat, multi batches of fermentation were performed. Results showed that the dextranase synthesis under GAP promoter is growth-associated and mainly in exponential phase and stationary phase. Activity of dextranase in 6.8 L, 50 L, 500 L and 5000 L fermenter reached 1253, 1300, 740 and 589 U/m L, respectively. A simple and convenient fermentation method using glycerol as carbon source has been developed, which obviates problems related with methanol safety concerns and is suitable for large scale production.
出处
《甘蔗糖业》
2016年第2期20-26,共7页
Sugarcane and Canesugar
基金
现代农业产业技术体系建设专项资金(CARS-20-4-5)
八桂学者建设工程专项经费
关键词
α-葡聚糖酶
毕赤酵母
组成型表达
发酵放大
Dextranase
Pichia pastoris
Constitutive expression
Fermentation scale-up