Suppr超能文献

利用高密度活细胞的产丁酸梭菌生产高速度、高效率但丁醇系统的开发。

Development of high-speed and highly efficient butanol production systems from butyric acid with high density of living cells of Clostridium saccharoperbutylacetonicum.

机构信息

Laboratory of Microbial Technology, Division of Applied Molecular Microbiology and Biomass Chemistry, Department of Bioscience and Biotechnology, Faculty of Agriculture, Graduate School, Kyushu University, 6-10-1 Hakozaki, Higashi-ku, Fukuoka 812-8581, Japan.

出版信息

J Biotechnol. 2012 Feb 20;157(4):605-12. doi: 10.1016/j.jbiotec.2011.06.004. Epub 2011 Jun 12.

Abstract

Living cells are alive and have the butanol-producing ability but not much proliferation under nitrogen source-limited condition. We investigated various butanol production systems with high density of living cells of Clostridium saccharoperbutylacetonicum N1-4 supplemented with methyl viologen (MV) as an electron carrier and nutrient dosing for activity regeneration. In continuous butanol production with high density of living cells, butanol yield was drastically increased from 0.365 C-mol/C-mol with growing cells to 0.528 C-mol/C-mol at a dilution rate of 0.85 h⁻¹, being increased with the butanol to total solvent ratio. This yield was increased to 0.591 C-mol/C-mol by adding 0.01 mM MV. MV addition increased not only butanol yield but also butanol concentration and productivity as compared to those without MV addition. However, living cells lost their activity with incubation time, which lowered the operational stability of the system. Therefore, to maintain constant stability, activity regeneration was carried out with high density of living cells and MV. This system produced butanol at high concentration (9.40 g l⁻¹) and productivity (7.99 g l⁻¹ h⁻¹) for approximately 100 h with maintenance of considerably high yield of butanol (0.686 C-mol/C-mol). Thus, we established a high-speed and highly efficient butanol production system.

摘要

在氮源有限的条件下,活细胞具有生产丁醇的能力,但增殖能力不强。我们研究了各种丁醇生产系统,这些系统使用添加了作为电子载体的甲紫精(MV)的高浓度的产丁醇梭菌(Clostridium saccharoperbutylacetonicum N1-4)细胞,并进行了营养物补料以实现活性再生。在高浓度活细胞的连续丁醇生产中,丁醇得率从生长细胞的 0.365 C-mol/C-mol 急剧增加到稀释率为 0.85 h⁻¹ 时的 0.528 C-mol/C-mol,并且随着丁醇与总溶剂的比例增加而增加。添加 0.01 mM MV 可将产率提高到 0.591 C-mol/C-mol。与不添加 MV 的情况相比,MV 的添加不仅提高了丁醇得率,而且提高了丁醇浓度和生产效率。然而,活细胞随着孵育时间的延长而失去活性,从而降低了系统的操作稳定性。因此,为了保持稳定,使用高浓度的活细胞和 MV 进行了活性再生。该系统在大约 100 小时内以高浓度(9.40 g l⁻¹)和高生产力(7.99 g l⁻¹ h⁻¹)生产丁醇,同时保持相当高的丁醇得率(0.686 C-mol/C-mol)。因此,我们建立了一个高速高效的丁醇生产系统。

文献检索

告别复杂PubMed语法,用中文像聊天一样搜索,搜遍4000万医学文献。AI智能推荐,让科研检索更轻松。

立即免费搜索

文件翻译

保留排版,准确专业,支持PDF/Word/PPT等文件格式,支持 12+语言互译。

免费翻译文档

深度研究

AI帮你快速写综述,25分钟生成高质量综述,智能提取关键信息,辅助科研写作。

立即免费体验