基于多元响应面分析的搅拌槽生物反应器中真菌青霉产纤维素酶优化研究。

Q2 Biochemistry, Genetics and Molecular Biology
Enzyme Research Pub Date : 2014-01-01 Epub Date: 2014-06-25 DOI:10.1155/2014/703291
Marcelle Lins de Albuquerque de Carvalho, Daniele Fernandes Carvalho, Edelvio de Barros Gomes, Roberto Nobuyuki Maeda, Lidia Maria Melo Santa Anna, Aline Machado de Castro, Nei Pereira
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引用次数: 26

摘要

对生产第二代乙醇的兴趣日益增加,需要从纤维素水解复合物(内切葡聚糖酶、外切葡聚糖酶和β-葡萄糖苷酶)中低成本生产酶,这些酶在纤维素分解中起协同作用。目前的工作旨在优化从真菌Penicillium funiculosum ATCC11797生产这些生物催化剂的生物工艺。采用统计全因子设计(FFD)确定纤维素酶生产的最佳条件。以Avicel (10 g·L(-1))为碳源,确定最佳培养基组成为尿素(1.2 g·L(-1))、酵母浸膏(1.0 g·L(-1))、KH2PO4 (6.0 g·L(-1))、MgSO4·7H2O (1.2 g·L(-1))。在生物反应器中分批进行生长过程。采用不同的FFD策略,优化的生物反应器操作条件为搅拌速度220 rpm,曝气率0.6 vvm,可获得FPase活性为508 U·L(-1),内切葡聚糖酶活性为9,204 U·L(-1), β-葡萄糖苷酶活性为2,395 U·L(-1)的酶池。顺序优化策略是有效的,与使用非优化条件相比,纤维素酶的产量增加了3.6到9.5倍。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Optimisation of Cellulase Production by Penicillium funiculosum in a Stirred Tank Bioreactor Using Multivariate Response Surface Analysis.

Optimisation of Cellulase Production by Penicillium funiculosum in a Stirred Tank Bioreactor Using Multivariate Response Surface Analysis.

Optimisation of Cellulase Production by Penicillium funiculosum in a Stirred Tank Bioreactor Using Multivariate Response Surface Analysis.

Optimisation of Cellulase Production by Penicillium funiculosum in a Stirred Tank Bioreactor Using Multivariate Response Surface Analysis.

Increasing interest in the production of second-generation ethanol necessitates the low-cost production of enzymes from the cellulolytic complex (endoglucanases, exoglucanases, and β-glucosidases), which act synergistically in cellulose breakdown. The present work aimed to optimise a bioprocess to produce these biocatalysts from the fungus Penicillium funiculosum ATCC11797. A statistical full factorial design (FFD) was employed to determine the optimal conditions for cellulase production. The optimal composition of culture media using Avicel (10 g·L(-1)) as carbon source was determined to include urea (1.2 g·L(-1)), yeast extract (1.0 g·L(-1)), KH2PO4 (6.0 g·L(-1)), and MgSO4 ·7H2O (1.2 g·L(-1)). The growth process was performed in batches in a bioreactor. Using a different FFD strategy, the optimised bioreactor operational conditions of an agitation speed of 220 rpm and aeration rate of 0.6 vvm allowed the obtainment of an enzyme pool with activities of 508 U·L(-1) for FPase, 9,204 U·L(-1) for endoglucanase, and 2,395 U·L(-1) for β-glucosidase. The sequential optimisation strategy was effective and afforded increased cellulase production in the order from 3.6 to 9.5 times higher than production using nonoptimised conditions.

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来源期刊
Enzyme Research
Enzyme Research Biochemistry, Genetics and Molecular Biology-Biochemistry
CiteScore
4.60
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