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2
Screening of non-Ionic Surfactant for Enhancing Biobutanol Production.
Appl Biochem Biotechnol. 2015 Nov;177(6):1272-81. doi: 10.1007/s12010-015-1812-y. Epub 2015 Aug 28.
3
Extractive microbial fermentation in cloud point system.浊点系统中的萃取微生物发酵
Enzyme Microb Technol. 2010 May 5;46(6):407-18. doi: 10.1016/j.enzmictec.2010.02.004. Epub 2010 Feb 13.
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Extraction of p-coumaric acid and ferulic acid using surfactant-based aqueous two-phase system.
Appl Biochem Biotechnol. 2014 Sep;174(2):564-73. doi: 10.1007/s12010-014-1107-8. Epub 2014 Aug 1.
5
Investigation of gas stripping and pervaporation for improved feasibility of two-stage butanol production process.研究气体汽提和渗透蒸发以提高两段丁醇生产工艺的可行性。
Bioresour Technol. 2013 May;136:102-8. doi: 10.1016/j.biortech.2013.02.046. Epub 2013 Feb 24.
6
Membrane-assisted extractive butanol fermentation by Clostridium saccharoperbutylacetonicum N1-4 with 1-dodecanol as the extractant.膜辅助提取丁醇发酵梭菌 saccharoperbutylacetonicum N1-4 与 1-十二醇作为萃取剂。
Bioresour Technol. 2012 Jul;116:448-52. doi: 10.1016/j.biortech.2012.03.096. Epub 2012 Apr 4.
7
High yield bio-butanol production by solvent-producing bacterial microflora.溶剂产生菌微生物群落高产生物丁醇的生产。
Bioresour Technol. 2012 Jun;113:58-64. doi: 10.1016/j.biortech.2011.12.133. Epub 2012 Jan 2.
8
In situ extraction of polar product of whole cell microbial transformation with polyethylene glycol-induced cloud point system.聚乙二醇诱导浊点系统原位萃取全细胞微生物转化的极性产物
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9
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.
10
Production of acetone butanol (AB) from liquefied corn starch, a commercial substrate, using Clostridium beijerinckii coupled with product recovery by gas stripping.利用拜氏梭菌从商业底物液化玉米淀粉中生产丙酮丁醇(AB),并通过气提进行产物回收。
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拜氏梭菌MCMB 581在选定表面活性剂存在下提高正丁醇产量

Enhanced n-butanol production by Clostridium beijerinckii MCMB 581 in presence of selected surfactant.

作者信息

Singh Kajal, Gedam Preety S, Raut Atulkumar N, Dhamole Pradip B, Dhakephalkar P K, Ranade Dilip R

机构信息

MACS-Agharkar Research Institute (ARI), G.G. Agharkar Road, Pune, Maharashtra, 411004, India.

Department of Chemical Engineering, Visvesvaraya National Institute of Technology, South Ambazari Road, Nagpur, Maharashtra, 440010, India.

出版信息

3 Biotech. 2017 Jul;7(3):161. doi: 10.1007/s13205-017-0803-9. Epub 2017 Jun 29.

DOI:10.1007/s13205-017-0803-9
PMID:28660448
原文链接:https://pmc.ncbi.nlm.nih.gov/articles/PMC5489445/
Abstract

Extractive butanol fermentation with non-ionic surfactant, a recently explored area, has shown promising results with several advantages but is relatively less investigated. This work reports the extractive fermentation with selected non-ionic surfactants (L62 and L62D) to enhance butanol production using a high-butanol producing strain (Clostridium beijerinckii MCMB 581). Biocompatibility studies with both the surfactants showed growth. Higher concentrations of surfactant (>5%) affected the cell count. 15.3 g L of butanol and 21 g L of total solvents were obtained with 3% (v/v) L62 which was respectively, 43% (w/w) and 55% (w/w), higher than control. It was found that surfactant addition at 9th h doubled the productivity (from 0.13 to 0.31 g L h and 0.17 to 0.39 g L h, respectively for butanol and total solvent). Butanol productivity obtained was 2-3 times higher than similar studies on extractive fermentation with non-ionic surfactants. Interestingly, mixing did not improve butanol production.

摘要

采用非离子表面活性剂进行萃取丁醇发酵是一个最近才探索的领域,已显示出有前景的结果,具有几个优点,但相对较少受到研究。这项工作报道了使用选定的非离子表面活性剂(L62和L62D)进行萃取发酵,以利用高产丁醇菌株(拜氏梭菌MCMB 581)提高丁醇产量。对这两种表面活性剂的生物相容性研究显示有生长现象。较高浓度的表面活性剂(>5%)影响细胞计数。使用3%(v/v)的L62获得了15.3 g/L的丁醇和21 g/L的总溶剂,分别比对照高43%(w/w)和55%(w/w)。发现第9小时添加表面活性剂使生产率提高了一倍(丁醇和总溶剂的生产率分别从0.13 g/L·h和0.17 g/L·h提高到0.31 g/L·h和0.39 g/L·h)。所获得的丁醇生产率比关于非离子表面活性剂萃取发酵的类似研究高2至3倍。有趣的是,混合并没有提高丁醇产量。