• 文献检索
  • 文档翻译
  • 深度研究
  • 学术资讯
  • Suppr Zotero 插件Zotero 插件
  • 邀请有礼
  • 套餐&价格
  • 历史记录
应用&插件
Suppr Zotero 插件Zotero 插件浏览器插件Mac 客户端Windows 客户端微信小程序
定价
高级版会员购买积分包购买API积分包
服务
文献检索文档翻译深度研究API 文档MCP 服务
关于我们
关于 Suppr公司介绍联系我们用户协议隐私条款
关注我们

Suppr 超能文献

核心技术专利:CN118964589B侵权必究
粤ICP备2023148730 号-1Suppr @ 2026

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

将有毒底物微生物转化为有毒产物的辅助相指南。

Auxiliary phase guidelines for microbial biotransformations of toxic substrate into toxic product.

作者信息

Straathof A J J

机构信息

Kluyver Laboratory for Biotechnology, Delft University of Technology, Julianalaan 67, 2628 BC Delft, The Netherlands.

出版信息

Biotechnol Prog. 2003 May-Jun;19(3):755-62. doi: 10.1021/bp025750m.

DOI:10.1021/bp025750m
PMID:12790635
Abstract

When an industrial process is developed using the microbial transformation of a precursor into a desired chemical compound, high concentrations of substrate and product will be involved. These compounds may become toxic to the cells. In situ product removal (ISPR) may be carried out, using auxiliary phases such as extractants or adsorbents. Simultaneously, in situ substrate addition (ISSA) may be performed. It is shown that for uncharged substrates and products, the aqueous solubilities of substrate and product can be used to predict if ISPR might be required. When a particular auxiliary phase is selected and the distribution coefficients of substrate and product are known, it is possible to estimate a priori if this auxiliary phase might be good enough and how much of it might be needed for an efficient (fed-)batch biotransformation process. For biotransformation products of intermediate polarity (aqueous solubility of about 1-10 g/L) there seems to be a lack of extractants and adsorbents with the capacity to raise the product concentrations to commercially more interesting levels.

摘要

当利用微生物将前体转化为所需化合物来开发工业过程时,会涉及高浓度的底物和产物。这些化合物可能对细胞产生毒性。可以使用萃取剂或吸附剂等辅助相进行原位产物去除(ISPR)。同时,可以进行原位底物添加(ISSA)。结果表明,对于不带电荷的底物和产物,可以使用底物和产物的水溶性来预测是否需要ISPR。当选择了特定的辅助相且已知底物和产物的分配系数时,就可以预先估计该辅助相是否足够好,以及对于高效的(补料)分批生物转化过程可能需要多少辅助相。对于中等极性的生物转化产物(水溶性约为1 - 10 g/L),似乎缺乏能够将产物浓度提高到更具商业价值水平的萃取剂和吸附剂。

相似文献

1
Auxiliary phase guidelines for microbial biotransformations of toxic substrate into toxic product.将有毒底物微生物转化为有毒产物的辅助相指南。
Biotechnol Prog. 2003 May-Jun;19(3):755-62. doi: 10.1021/bp025750m.
2
Evaluation of kinetic models for industrial acetic fermentation: proposal of a new model optimized by genetic algorithms.工业醋酸发酵动力学模型的评估:一种通过遗传算法优化的新模型的提议。
Biotechnol Prog. 2003 Mar-Apr;19(2):599-611. doi: 10.1021/bp0256871.
3
Industrial potential of organic solvent tolerant bacteria.耐有机溶剂细菌的工业潜力。
Biotechnol Prog. 2004 May-Jun;20(3):655-60. doi: 10.1021/bp0200595.
4
In situ product recovery (ISPR) by crystallization: basic principles, design, and potential applications in whole-cell biocatalysis.通过结晶进行原位产物回收(ISPR):基本原理、设计及其在全细胞生物催化中的潜在应用
Appl Microbiol Biotechnol. 2006 Jun;71(1):1-12. doi: 10.1007/s00253-006-0378-6. Epub 2006 Apr 11.
5
The snowball effect in fed-batch bioreactions.补料分批生物反应中的雪球效应。
Biotechnol Prog. 2003 May-Jun;19(3):1064-70. doi: 10.1021/bp025792a.
6
Batch kinetics of Pseudomonas sp. growth on benzene. Modeling of product and substrate inhibitions.假单胞菌在苯上生长的批次动力学。产物和底物抑制的建模。
Biotechnol Prog. 2003 Mar-Apr;19(2):676-9. doi: 10.1021/bp025764s.
7
Conversion of a CHO cell culture process from perfusion to fed-batch technology without altering product quality.在不改变产品质量的情况下,将CHO细胞培养工艺从灌注技术转换为补料分批技术。
J Biotechnol. 2006 May 3;123(1):106-16. doi: 10.1016/j.jbiotec.2005.10.013. Epub 2005 Dec 1.
8
Feedback stabilization of fed-batch bioreactors: non-monotonic growth kinetics.补料分批式生物反应器的反馈稳定:非单调生长动力学
Biotechnol Prog. 2002 Sep-Oct;18(5):1116-25. doi: 10.1021/bp010191p.
9
Solvent toxicity in organic-aqueous systems analysed by multivariate analysis.通过多变量分析对有机-水体系中的溶剂毒性进行分析。
Bioprocess Biosyst Eng. 2004 Dec;26(6):361-75. doi: 10.1007/s00449-004-0381-1. Epub 2004 Sep 17.
10
Bioprocess control from a multivariate process trajectory.基于多变量过程轨迹的生物过程控制。
Bioprocess Biosyst Eng. 2004 Dec;26(6):401-11. doi: 10.1007/s00449-003-0327-z. Epub 2003 Sep 5.

引用本文的文献

1
Efficient synthesis of enantiopure amines from alcohols using resting cells and ammonia.利用静息细胞和氨从醇类高效合成对映体纯胺类。
Green Chem. 2019 Jul 14;21(14):3846-3857. doi: 10.1039/C9GC01059A. Epub 2019 Jun 25.
2
Bioconversion of L-phenylalanine to 2-phenylethanol by the novel stress-tolerant yeast Candida glycerinogenes WL2002-5.新型耐胁迫酵母甘油克鲁维酵母WL2002-5将L-苯丙氨酸生物转化为2-苯乙醇
Bioengineered. 2016 Nov;7(6):418-423. doi: 10.1080/21655979.2016.1171437. Epub 2016 Jul 19.
3
Whole cell biocatalysts: essential workers from Nature to the industry.
全细胞生物催化剂:从自然界到工业界的重要参与者。
Microb Biotechnol. 2017 Mar;10(2):250-263. doi: 10.1111/1751-7915.12363. Epub 2016 May 3.
4
Solubilization capacity of nonionic surfactant micelles exhibiting strong influence on export of intracellular pigments in Monascus fermentation.非离子表面活性剂胶束的增溶能力对红曲菌发酵中细胞内色素的外排有很大的影响。
Microb Biotechnol. 2013 Sep;6(5):540-50. doi: 10.1111/1751-7915.12039. Epub 2013 Feb 20.
5
Integrated bioprocess for the stereospecific production of linalool oxides from linalool with Corynespora cassiicola DSM 62475.利用棒形青霉菌(Corynespora cassiicola DSM 62475)从芳樟醇立体特异性生产芳樟醇氧化物的综合生物工艺。
J Ind Microbiol Biotechnol. 2012 Dec;39(12):1761-9. doi: 10.1007/s10295-012-1181-2. Epub 2012 Aug 18.
6
Fermentative production of isobutene.异丁烯的发酵生产。
Appl Microbiol Biotechnol. 2012 Feb;93(4):1377-87. doi: 10.1007/s00253-011-3853-7. Epub 2012 Jan 11.
7
Whole cell microbial transformation in cloud point system.浊点体系中的全细胞微生物转化
J Ind Microbiol Biotechnol. 2008 Jul;35(7):645-56. doi: 10.1007/s10295-008-0345-6. Epub 2008 Apr 8.