High Cell Density Cultivation of Pseudomonas putida KT2440 Using Glucose Without the Need for Oxygen Enriched Air Supply

被引:58
作者
Davis, Reeta [1 ,2 ]
Duane, Gearoid [3 ]
Kenny, Shane T. [1 ]
Cerrone, Federico [1 ,2 ]
Guzik, Maciej W. [1 ]
Babu, Ramesh P. [2 ,4 ]
Casey, Eoin [3 ]
O'Connor, Kevin E. [1 ,2 ]
机构
[1] Univ Coll Dublin, Sch Biomol & Biomed Sci, Dublin 4, Ireland
[2] Natl Univ Ireland, Technol Ctr Biorefining & Bioenergy, Galway, Ireland
[3] Univ Coll Dublin, Sch Chem & Bioproc Engn, Dublin 4, Ireland
[4] Univ Dublin Trinity Coll, Sch Phys, Dublin 2, Ireland
关键词
bioprocess engineering; modeling; Pseudomonas putida KT2440; fed-batch; glucose; polyhydroxyalkanoates; CHAIN-LENGTH POLYHYDROXYALKANOATES; FED-BATCH CULTIVATION; ESCHERICHIA-COLI; ACID; TOLERANCE; EFFICIENT;
D O I
10.1002/bit.25474
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
High Cell Density (HCD) cultivation of bacteria is essential for the majority of industrial processes to achieve high volumetric productivity (gL(-1) h(-1)) of a bioproduct of interest. This study developed a fed batch bioprocess using glucose as sole carbon and energy source for the HCD of the well described biocatalyst Pseudomonas putida KT2440 without the supply of oxygen enriched air. Growth kinetics data from batch fermentations were used for building a bioprocess model and designing feeding strategies. An exponential followed by linearly increasing feeding strategy of glucose was found to be effective in maintaining biomass productivity while also delaying the onset of dissolved oxygen (supplied via compressed air) limitation. A final cell dry weight (CDW) of 102gL(-1) was achieved in 33h with a biomass productivity of 3.1gL(-1) h(-1) which are the highest ever reported values for P. putida strains using glucose without the supply of pure oxygen or oxygen enriched air. The usefulness of the biomass as a biocatalyst was demonstrated through the production of the biodegradable polymer polyhydroxyalkanoate (PHA). When nonanoic acid (NA) was supplied to the glucose grown cells of P. putida KT2440, it accumulated 32% of CDW as PHA in 11h (2.85gL(-1) h(-1)) resulting in a total of 0.56kg of PHA in 18L with a yield of 0.56g PHA g NA(-1). Biotechnol. Bioeng. 2015;112: 725-733. (c) 2014 Wiley Periodicals, Inc.
引用
收藏
页码:725 / 733
页数:9
相关论文
共 41 条
[1]   Glucose/lipid mixed substrates as a means of controlling the properties of medium chain length poly(hydroxyalkanoates) [J].
Ashby, RD ;
Solaiman, DKY ;
Foglia, TA ;
Liu, CK .
BIOMACROMOLECULES, 2001, 2 (01) :211-216
[2]   Enzymatic hydrolysis of corn starch after extraction of corn oil with ethanol [J].
Cao, NG ;
Xu, Q ;
Ni, JL ;
Chen, LF .
APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, 1996, 57-8 :39-47
[3]   Efficient production of soluble recombinant single chain Fv fragments by a Pseudomonas putida strain KT2440 cell factory [J].
Dammeyer, Thorben ;
Steinwand, Miriam ;
Krueger, Sarah-C ;
Duebel, Stefan ;
Hust, Michael ;
Timmis, Kenneth N. .
MICROBIAL CELL FACTORIES, 2011, 10
[4]   Role of (R)-specific enoyl coenzyme A hydratases of Pseudomonas sp in the production of polyhydroxyalkanoates [J].
Davis, Reeta ;
Chandrashekar, Arun ;
Shamala, Tumkur R. .
ANTONIE VAN LEEUWENHOEK INTERNATIONAL JOURNAL OF GENERAL AND MOLECULAR MICROBIOLOGY, 2008, 93 (03) :285-296
[5]   Conversion of grass biomass into fermentable sugars and its utilization for medium chain length polyhydroxyalkanoate (mcl-PHA) production by Pseudomonas strains [J].
Davis, Reeta ;
Kataria, Rashmi ;
Cerrone, Federico ;
Woods, Trevor ;
Kenny, Shane ;
O'Donovan, Anthonia ;
Guzik, Maciej ;
Shaikh, Hamid ;
Duane, Gearoid ;
Gupta, Vijai Kumar ;
Tuohy, Maria G. ;
Padamatti, Ramesh Babu ;
Casey, Eoin ;
O'Connor, Kevin E. .
BIORESOURCE TECHNOLOGY, 2013, 150 :202-209
[6]   High-cell-density cultivation of Pseudomonas putida IPT 046 and medium-chain-length polyhydroxyalkanoate production from sugarcane carbohydrates [J].
Diniz, SC ;
Taciro, MK ;
Gomez, JGC ;
Pradella, JGD .
APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, 2004, 119 (01) :51-69
[7]  
Doran Pauline M., 1995, Bioprocess Engineering Principles
[8]   Large-Scale Production of Poly(3-Hydroxyoctanoic Acid) by Pseudomonas putida GPo1 and a Simplified Downstream Process [J].
Elbahloul, Yasser ;
Steinbuechel, Alexander .
APPLIED AND ENVIRONMENTAL MICROBIOLOGY, 2009, 75 (03) :643-651
[9]  
Enfors S.O., 2000, Bioprocess Technology Fundamentals and Applications
[10]   Putting cells under pressure: A simple and efficient way to enhance the productivity of medium-chain-length polyhydroxyalkanoate in processes with Pseudomonas putida KT2440 [J].
Follonier, Stephanie ;
Henes, Bernhard ;
Panke, Sven ;
Zinn, Manfred .
BIOTECHNOLOGY AND BIOENGINEERING, 2012, 109 (02) :451-461