Enhancing polyhydroxybutyrate production from high cell density fed-batch fermentation of Bacillus megaterium BA-019

被引:39
|
作者
Kanjanachumpol, Pawut [1 ]
Kulpreecha, Songsri [1 ]
Tolieng, Vasana [2 ]
Thongchul, Nuttha [2 ]
机构
[1] Chulalongkorn Univ, Dept Microbiol, Fac Sci, Bangkok 10330, Thailand
[2] Chulalongkorn Univ, Inst Biotechnol & Genet Engn, Bangkok 10330, Thailand
关键词
Polyhydroxybutyrate; High cell density production; Fed-batch cultivation; Fermentation scale-up; Sugarcane molasses; Bacillus megaterium; POLY-BETA-HYDROXYBUTYRATE; ACTIVATED-SLUDGE; CANE MOLASSES; SCALE-UP; BACTERIAL; POLYHYDROXYALKANOATES; PHB; CARBON; BIOSYNTHESIS; CULTIVATION;
D O I
10.1007/s00449-013-0885-7
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
This study demonstrated the improved polyhydroxybutyrate (PHB) production via high cell density cultivation of Bacillus megaterium BA-019 with balanced initial total sugar concentration and carbon to nitrogen (C/N) weight ratio. In the 10 L stirred fermentor operated at 30 A degrees C, pH 7.0, 600 rpm, and 1.0 vvm air, with the initial total sugar concentration of 60 g/L and urea at the C/N weight ratio of 10:1, 32.48 g/L cell biomass with the corresponding PHB weight content of 26.94 % and volumetric productivity of 0.73 g/L h were obtained from batch cultivation. Continuing cultivation by intermittent feeding of the sugarcane molasses along with urea at the C/N weight ratio of 12.5:1 gave much improved biomass and PHB production (90.71 g/L biomass with 45.84 % PHB content and 1.73 g/L h PHB productivity). Similar biomass and PHB yields were obtained in the 90 L stirred fermentor when using the impeller tip speed as the scale-up criterion.
引用
收藏
页码:1463 / 1474
页数:12
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