High-cell-density poly (3-hydroxybutyrate) production from sucrose using Burkholderia sacchari culture in airlift bioreactor

被引:32
作者
da Cruz Pradella, Jose Geraldo [1 ]
Taciro, Marilda Keico [2 ]
Pataquiva Mateus, Alis Yovana [2 ]
机构
[1] Lab Nacl Ciencia & Tecnol, BR-13083970 Campinas, SP, Brazil
[2] Inst Pesquisas Tecnol Estado Sao Paulo SA, BR-0508901 Sao Paulo, Brazil
关键词
Airlift bioreactor; Poly (3-hydroxybutyrate); High-cell-density; POLYHYDROXYALKANOATE PRODUCTION; BACTERIAL FERMENTATION; POLY(3-HYDROXYBUTYRATE-CO-3-HYDROXYVALERATE); ECONOMICS;
D O I
10.1016/j.biortech.2010.05.046
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Burkholderia sacchari IPT 189 poly (3-hydroxybutyrate) (P3HB) production in airlift bioreactor were investigated in batch and fed-batch culture using sucrose as carbon source. In batch experiments it was observed that during the growth phase B. sacchari IPT 189 might display exponential growth even at very low carbohydrate concentration, as long as NH(4)(+) concentration was above 190 mg l(-1). The onset of accumulation phase took place when NH(4)(+) concentration dropped below this value and continued as long as carbohydrate was in excess, even with dissolved oxygen concentration at 0.0% of air saturation. In the fed-batch experiments, nitrogen limitation was used to induce P3HB biosynthesis in a two-phase process. In the first phase, an initial batch followed by a limited sucrose fed regime led to a growth with low-P3HB-content (less than 13%) and up to 60 gl(-1) of biomass concentration in ca. 25 h. In the second phase, nitrogen concentration limitation induced P3HB accumulation up to 42%, raising the biomass concentration to c.a. 150 gl(-1). Calculated parameters for the experiments were P3HB productivity = 1.7 gl(-1) h(-1) and P3HB yield factor from sucrose = 0.22 g g(-1). (C) 2010 Elsevier Ltd. All rights reserved.
引用
收藏
页码:8355 / 8360
页数:6
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