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用于生产和回收羟基四氢嘧啶的海洋球菌M52的高产培养

High-yield cultivation of Marinococcus M52 for production and recovery of hydroxyectoine.

作者信息

Schiraldi Chiara, Maresca Carmelina, Catapano Angela, Galinski Erwin A, De Rosa Mario

机构信息

Department of Experimental Medicine, Section of Biotechnology and Molecular Biology, Second University of Naples, via De Crecchio no. 7, 80138 Naples, Italy.

出版信息

Res Microbiol. 2006 Sep;157(7):693-9. doi: 10.1016/j.resmic.2006.03.004. Epub 2006 Apr 4.

Abstract

Ectoine and hydroxyectoine, produced by Halomonas ssp. and Marinococcus ssp., have been extensively characterized and proposed for biotechnological applications. Large-scale production of ectoine was achieved by implementing the so-called "milking process" by Bitop (Witten, Germany) and commercializing compatible solutes as stabilizers for biological systems. However, there is a continuing interest in optimization of the production process for hydroxyectoine alone, as the latter was shown to have greater stabilization capacity. Recently, Marinococcus strain M52 was selected for its ability to convert most ectoine into hydroxyectoine during a prolonged stationary phase. This study reports on the correlation between growth conditions and hydroxyectoine production in Marinococcus M52 cultivation. We demonstrated that a dissolved oxygen content higher than 10% during cultivation leads to more rapid accumulation of hydroxyectoine than of ectoine (with hydroxyectoine up to 1.6 g l-1). In addition, we employed a microfiltration bioprocess to improve biomass and yield of products (reaching 3.6 g l-1 of hydroxyectoine). Finally, we developed a novel extraction method based on osmotic down-shock coupled with thermal permeabilization to recover the desired products from the biomass.

摘要

由嗜盐单胞菌属(Halomonas ssp.)和海球菌属(Marinococcus ssp.)产生的四氢嘧啶和羟基四氢嘧啶已得到广泛表征,并被提议用于生物技术应用。德国维滕的Bitop公司通过实施所谓的“挤奶工艺”实现了四氢嘧啶的大规模生产,并将相容性溶质作为生物系统的稳定剂进行商业化。然而,由于羟基四氢嘧啶显示出更大的稳定能力,人们一直对单独优化其生产工艺感兴趣。最近,海球菌菌株M52因其在延长的稳定期内将大部分四氢嘧啶转化为羟基四氢嘧啶的能力而被选中。本研究报告了海球菌M52培养过程中生长条件与羟基四氢嘧啶产量之间的相关性。我们证明,培养过程中溶解氧含量高于10%时,羟基四氢嘧啶的积累比四氢嘧啶更快(羟基四氢嘧啶含量高达1.6 g l-1)。此外,我们采用微滤生物工艺提高了生物量和产物产量(羟基四氢嘧啶达到3.6 g l-1)。最后,我们开发了一种基于渗透降冲击与热渗透相结合的新型提取方法,以从生物质中回收所需产物。

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