Chan Sitha, Jantama Sirima Suvarnakuta, Kanchanatawee Sunthorn, Jantama Kaemwich
Metabolic Engineering Research Unit, School of Biotechnology, Institute of Agricultural Technology, Suranaree University of Technology, 111 University Ave., Suranaree Sub-district, Muang District, Nakhon Ratchasima, 30000, Thailand.
Division of Biopharmacy, Faculty of Pharmaceutical Sciences, Ubon Ratchathani University, Warinchamrap, Ubon Ratchathani, 34190, Thailand.
PLoS One. 2016 Sep 7;11(9):e0161503. doi: 10.1371/journal.pone.0161503. eCollection 2016.
An optimization process with a cheap and abundant substrate is considered one of the factors affecting the price of the production of economical 2,3-Butanediol (2,3-BD). A combination of the conventional method and response surface methodology (RSM) was applied in this study. The optimized levels of pH, aeration rate, agitation speed, and substrate concentration (maltodextrin) were investigated to determine the cost-effectiveness of fermentative 2,3-BD production by metabolically-engineered Klebsiella oxytoca KMS005. Results revealed that pH, aeration rate, agitation speed, and maltodextrin concentration at levels of 6.0, 0.8 vvm, 400 rpm, and 150 g/L respectively were the optimal conditions. RSM also indicated that the agitation speed was the most influential parameter when either agitation and aeration interaction or agitation and substrate concentration interaction played important roles for 2,3-BD production by the strain from maltodextrin. Under interim fed-batch fermentation, 2,3-BD concentration, yield, and productivity were obtained at 88.1±0.2 g/L, 0.412±0.001 g/g, and 1.13±0.01 g/L/h respectively within 78 h.
使用廉价且丰富的底物的优化过程被认为是影响经济生产2,3-丁二醇(2,3-BD)成本的因素之一。本研究采用了传统方法与响应面法(RSM)相结合的方式。研究了pH值、通气速率、搅拌速度和底物浓度(麦芽糊精)的优化水平,以确定代谢工程改造的产酸克雷伯菌KMS005发酵生产2,3-BD的成本效益。结果表明,pH值为6.0、通气速率为0.8 vvm、搅拌速度为400 rpm、麦芽糊精浓度为150 g/L时为最佳条件。响应面法还表明,当搅拌与通气相互作用或搅拌与底物浓度相互作用对该菌株利用麦芽糊精生产2,3-BD起重要作用时,搅拌速度是最具影响力的参数。在间歇补料分批发酵条件下,78小时内2,3-BD浓度、产量和生产率分别达到88.1±0.2 g/L、0.412±0.001 g/g和1.13±0.01 g/L/h。