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开发一种新型的利用乳糖作为底物联产β-半乳糖苷酶和乙醇的集成工艺。

Development of a novel integrated process for co-production of β-galactosidase and ethanol using lactose as substrate.

机构信息

Chemical Engineering Research Center, School of Chemical Engineering and Technology, Tianjin University, Tianjin 300072, PR China.

Chemical Engineering Research Center, School of Chemical Engineering and Technology, Tianjin University, Tianjin 300072, PR China; State Key Laboratory of Chemical Engineering, Tianjin University, Tianjin 300072, PR China; Collaborative Innovation Center of Chemical Science and Engineering (Tianjin), Tianjin 300072, PR China; Tianjin Key Laboratory of Membrane Science and Desalination Technology, Tianjin University, Tianjin 300072, PR China.

出版信息

Bioresour Technol. 2017 Apr;230:15-23. doi: 10.1016/j.biortech.2017.01.019. Epub 2017 Jan 12.

Abstract

A novel integrated process was developed successfully for co-production of β-galactosidase and ethanol using lactose as substrate, containing fermentation (Kluyveromyces lactis), isolation, permeabilization (a new recycling process) and spray drying. Firstly, a new fed-batch strategy optimized co-produced β-galactosidase at 105.91U/mL and ethanol at 32.16mg/mL, 4.40-fold and 10.82-fold increase over the results from initial conditions, respectively. Then a new mathematic model for the recycling permeabilization was established successfully. As expected, the total cells sediment from isolation of the fed-batch culture was permeabilized completely by distilled ethanol from broth supernatant. More amazedly, the specific activity of β-galactosidase product by spray drying the permeabilized cells reached 2.61U/mg, meeting the demand of commercial products. Furthermore, the ethanol product at 33.8% (v/v) was obtained from the novel integrated process, which could be applied for various applications. To conclude, the novel integrated process might be a feasible strategy to scale up for industrialization.

摘要

成功开发了一种新型的综合工艺,用于使用乳糖作为底物共生产β-半乳糖苷酶和乙醇,该工艺包括发酵(乳酸克鲁维酵母)、分离、渗透(一种新的回收工艺)和喷雾干燥。首先,采用新的补料分批策略,将共生产的β-半乳糖苷酶优化至 105.91U/mL,乙醇优化至 32.16mg/mL,分别比初始条件下的结果提高了 4.40 倍和 10.82 倍。然后成功建立了新的回收渗透过程的数学模型。正如预期的那样,从补料分批培养物分离得到的总细胞用来自发酵液上清液的蒸馏乙醇完全渗透。更令人惊讶的是,喷雾干燥渗透细胞得到的β-半乳糖苷酶产物的比活达到 2.61U/mg,满足了商业产品的需求。此外,新型综合工艺还可以从新型综合工艺中获得 33.8%(v/v)的乙醇产物,可应用于各种应用。总之,新型综合工艺可能是一种可行的工业化放大策略。

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