机构地区:[1]Heilongjiang Key Laboratory of Microbiology, College of Life Science, Heilongjiang University
出 处:《Agricultural Science & Technology》2014年第5期779-784,共6页农业科学与技术(英文版)
基 金:Supported by Educational Commission of Heilongjiang Province of China(11551z011)
摘 要:In order to improve the yield of β-mannase and to investigate the rules of fermentation production, a high-yield β-mannase producing strain, Bacillus licheniformis HDYM-04, was used to investigate the kinetics models based on the optimal fermentation conditions: HDYM-04 strain was fermented at 37℃ for 30 h with agitation speed at 300 r/min and aeration rate at 3 L/min in a 5 L fermenter, the initial addition amount of konjac flour was 2%(w/v), the initial pH of medium was 8.0, and the inoculum concentration was 6.7%(v/v). Three batch fermentation kinetic models were established (cell growth kinetic model, substrate consumption kinetic model, product formation kinetic model) bases on Logistic and Luedeking-Piret equations. To be specific, cell growth kinetic model was dX/dt =0.431X (1- X/ 15.522 ), substrate consumption kinetic model was -ds/dt =1.11 dX/dt +0.000 2 dP/dt +0.000 8X, and product formation kinetic model was dP/dt=133.1 dX +222.87X. The correlation coefficients R^2 of the three equations were 0.990 21, 0.989 08 and 0.988 12, respectively, which indicated a good correlation between experimental values and models. Therefore, the three equations could be used to describe the processes of cell growth, enzyme synthesis and substrate consumption during batch fermentation using B. licheniformis strain HDYM-04. The establishment of batch fermentation kinetic models (cell growth kinetic model, substrate depletion kinetic model, product formation kinetic model) could lay the theoretical foundation and provide practical reference for the applica- tion of HDYM-04 in fermentation industry.In order to improve the yield of β-mannase and to investigate the rules of fermentation production, a high-yield β-mannase producing strain, Bacillus licheniformis HDYM-04, was used to investigate the kinetics models based on the optimal fermentation conditions: HDYM-04 strain was fermented at 37℃ for 30 h with agitation speed at 300 r/min and aeration rate at 3 L/min in a 5 L fermenter, the initial addition amount of konjac flour was 2%(w/v), the initial pH of medium was 8.0, and the inoculum concentration was 6.7%(v/v). Three batch fermentation kinetic models were established(cell growth kinetic model, substrate consumption kinetic model,product formation kinetic model) bases on Logistic and Luedeking-Piret equations.To be specific, cell growth kinetic model wasdX dt=0.431X(1-X15.522), substrate consumption kinetic model was-dS dt=1.11dX dt+0.000 2dP dt+0.000 8X, and product formation kinetic model wasdP dt=133.1dX dt+222.87X. The correlation coefficients R2of the three equations were 0.990 21, 0.989 08 and 0.988 12, respectively, which indicated a good correlation between experimental values and models. Therefore,the three equations could be used to describe the processes of cell growth, enzyme synthesis and substrate consumption during batch fermentation using B. licheniformis strain HDYM-04. The establishment of batch fermentation kinetic models(cell growth kinetic model, substrate depletion kinetic model, product formation kinetic model)could lay the theoretical foundation and provide practical reference for the application of HDYM-04 in fermentation industry.
关 键 词:Bacillus licheniformis Β-MANNANASE Fermentation kinetics Batch fermentation
分 类 号:TQ920.1[轻工技术与工程—发酵工程]
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