Choi J I, Lee S Y
Department of Chemical Engineering and BioProcess Engineering Research Center, Korea Advanced Institute of Science and Technology, 373-1, Kusong-dong, Yusong-gu, Taejon 305-701, Korea.
Appl Environ Microbiol. 1999 Oct;65(10):4363-8. doi: 10.1128/AEM.65.10.4363-4368.1999.
Fermentation strategies for production of high concentrations of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [P(3HB-co-3HV)] with different 3-hydroxyvalerate (3HV) fractions by recombinant Escherichia coli harboring the Alcaligenes latus polyhydroxyalkanoate biosynthesis genes were developed. Fed-batch cultures of recombinant E. coli with the pH-stat feeding strategy facilitated production of high concentrations and high contents of P(3HB-co-3HV) in a chemically defined medium. When a feeding solution was added in order to increase the glucose and propionic acid concentrations to 20 g/liter and 20 mM, respectively, after each feeding, a cell dry weight of 120.3 g/liter and a relatively low P(3HB-co-3HV) content, 42.5 wt%, were obtained. Accumulation of a high residual concentration of propionic acid in the medium was the reason for the low P(3HB-co-3HV) content. An acetic acid induction strategy was used to stimulate the uptake and utilization of propionic acid. When a fed-batch culture and this strategy were used, we obtained a cell concentration, a P(3HB-co-3HV) concentration, a P(3HB-co-3HV) content, and a 3HV fraction of 141.9 g/liter, 88.1 g/liter, 62.1 wt%, and 15.3 mol%, respectively. When an improved nutrient feeding strategy, acetic acid induction, and oleic acid supplementation were used, we obtained a cell concentration, a P(3HB-co-3HV) concentration, a P(3HB-co-3HV) content, and a 3HV fraction of 203.1 g/liter, 158.8 g/liter, 78.2 wt%, and 10.6 mol%, respectively; this resulted in a high level of productivity, 2.88 g of P(3HB-co-3HV)/liter-h.
利用携带产碱杆菌聚羟基链烷酸生物合成基因的重组大肠杆菌,开发了生产不同3-羟基戊酸(3HV)组分的高浓度聚(3-羟基丁酸酯-co-3-羟基戊酸酯)[P(3HB-co-3HV)]的发酵策略。采用pH值控制补料策略对重组大肠杆菌进行补料分批培养,有助于在化学成分确定的培养基中生产高浓度、高含量的P(3HB-co-3HV)。每次补料后添加补料溶液,使葡萄糖和丙酸浓度分别增加到20 g/升和20 mM时,细胞干重为120.3 g/升,P(3HB-co-3HV)含量相对较低,为42.5 wt%。培养基中丙酸残留浓度较高是P(3HB-co-3HV)含量低的原因。采用乙酸诱导策略来刺激丙酸的摄取和利用。当使用补料分批培养和该策略时,我们分别获得了细胞浓度、P(3HB-co-3HV)浓度、P(3HB-co-3HV)含量和3HV组分,分别为141.9 g/升、88.1 g/升、62.1 wt%和15.3 mol%。当采用改进的营养补料策略、乙酸诱导和油酸补充时,我们分别获得了细胞浓度、P(3HB-co-3HV)浓度、P(3HB-co-3HV)含量和3HV组分,分别为203.1 g/升、158.8 g/升、78.2 wt%和10.6 mol%;这导致了较高的生产率,即2.88 g P(3HB-co-3HV)/升·小时。