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Production of medium-chain-length polyhydroxyalkanoates by sequential feeding of xylose and octanoic acid in engineered Pseudomonas putida KT2440
被引:77
作者:
Le Meur, Sylvaine
[1
]
Zinn, Manfred
[1
,2
]
Egli, Thomas
[3
]
Thoeny-Meyer, Linda
[1
]
Ren, Qun
[1
]
机构:
[1] Swiss Fed Labs Mat Sci & Technol Empa, Lab Biomat, CH-9014 St Gallen, Switzerland
[2] HES SO Valais Wallis, CH-1950 Sion, Switzerland
[3] Swiss Fed Inst Aquat Sci & Technol Eawag, CH-8600 Dubendorf, Switzerland
来源:
关键词:
mcl-PHA;
Xylose;
Octanoic acid;
Pseudomonas putida KT2440;
Sequential-feeding;
Tailor-made PHA;
RECOMBINANT ESCHERICHIA-COLI;
BETA-HYDROXYBUTYRIC ACID;
POLY(3-HYDROXYBUTYRATE) PRODUCTION;
ETHANOL-PRODUCTION;
NONANOIC ACID;
BATCH;
BIOSYNTHESIS;
GLUCOSE;
POLY(3-HYDROXYALKANOATES);
POLY(HYDROXYALKANOATES);
D O I:
10.1186/1472-6750-12-53
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:
Background: Pseudomonas putida KT2440 is able to synthesize large amounts of medium-chain-length polyhydroxyalkanoates (mcl-PHAs). To reduce the substrate cost, which represents nearly 50% of the total PHA production cost, xylose, a hemicellulose derivate, was tested as the growth carbon source in an engineered P. putida KT2440 strain. Results: The genes encoding xylose isomerase (XylA) and xylulokinase (XylB) from Escherichia coli W3110 were introduced into P. putida KT2440. The recombinant KT2440 exhibited a XylA activity of 1.47 U and a XylB activity of 0.97 U when grown on a defined medium supplemented with xylose. The cells reached a maximum specific growth rate of 0.24 h(-1) and a final cell dry weight (CDW) of 2.5 g L-1 with a maximal yield of 0.5 g CDW g(-1) xylose. Since no mcl-PHA was accumulated from xylose, mcl-PHA production can be controlled by the addition of fatty acids leading to tailor-made PHA compositions. Sequential feeding strategy was applied using xylose as the growth substrate and octanoic acid as the precursor for mcl-PHA production. In this way, up to 20% w w(-1) of mcl-PHA was obtained. A yield of 0.37 g mcl-PHA per g octanoic acid was achieved under the employed conditions. Conclusions: Sequential feeding of relatively cheap carbohydrates and expensive fatty acids is a practical way to achieve more cost-effective mcl-PHA production. This study is the first reported attempt to produce mcl-PHA by using xylose as the growth substrate. Further process optimizations to achieve higher cell density and higher productivity of mcl-PHA should be investigated. These scientific exercises will undoubtedly contribute to the economic feasibility of mcl-PHA production from renewable feedstock.
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