Enhanced yield of medium-chain-length polyhydroxyalkanoates from nonanoic acid by co-feeding glucose in carbon-limited, fed-batch culture

被引:34
作者
Sun, Zhiyong [2 ]
Ramsay, Juliana [2 ]
Guay, Martin [2 ]
Ramsay, Bruce [1 ]
机构
[1] Polyferm Canada Inc, Harrowsmith, ON K0H 1V0, Canada
[2] Queens Univ, Dept Chem Engn, Kingston, ON K7L 3N6, Canada
关键词
Medium-chain-length; Polyhydroxyalkanoate; Fed-batch; Fermentation; Pseudomonas putida; PHA; MCL-PHA; PSEUDOMONAS-PUTIDA KT2440; CELL-DENSITY CULTIVATION; ECONOMIC-EVALUATION; MCL-PHA; POLY(3-HYDROXYALKANOATES); FERMENTATION; OLEOVORANS; OCTANOATE;
D O I
10.1016/j.jbiotec.2009.07.014
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
Medium-chain-length polyhydroxyalkanoates (MCL-PHAs) were produced in carbon-limited, single-stage, fed-batch fermentations of Pseudomonas putida KT2440 by co-feeding nonanoic acid (NA) and glucose (G) to enhance the yield of PHA from NA. An exponential (mu = 0.25 h(-1)) followed by a linear feeding strategy at a NA:G ratio of 1:1 (w/w) achieved 71 gl(-1) biomass containing 56% PHA. Although the same overall PHA productivity (1.44 gl(-1) h(-1)) was obtained when NA alone was fed at the same specific growth rate, the overall yield of PHA from NA increased by 25% (0.66 g PHA g NA(-1) versus 0.53 gg(-1)) with glucose co-feeding. Further increasing glucose in the feed (NA:G=1:1.5) resulted in a slightly higher yield (0.69gPHAgNA(-1)) but lower PHA content (48%) and productivity (1.16gl(-1) h(-1)). There was very little change in the PHA composition. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:262 / 267
页数:6
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