Imidazolium ionic liquids-based salting-out extraction of 2,3-butanediol from fermentation broths

被引:19
|
作者
Dai, Jianying [1 ]
Wang, Hui [1 ]
Li, Yan [1 ]
Xiu, Zhi-Long [1 ]
机构
[1] Dalian Univ Technol, Sch Life Sci & Biotechnol, Dalian 116024, Peoples R China
基金
中国国家自然科学基金;
关键词
Salting-out extraction; 2,3-butanediol; Ionic liquids; Partition behavior; Fermentation broth; AQUEOUS BIPHASIC SYSTEMS; HYDROGEN-BOND ACIDITY; MICROBIAL-PRODUCTION; 2-PHASE EXTRACTION; SEPARATION PROCESSES; RENEWABLE RESOURCES; 1,3-PROPANEDIOL; HYDROLYSATE; MISCIBILITY; BIOPROCESS;
D O I
10.1016/j.procbio.2018.05.015
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
Salting-out extraction is an efficient technique for the separation of bio-based chemicals from fermentation broths. So far, salting-out extraction of 2,3-butanediol has mainly focused on systems composed of organic solvents and salts, while less attention has been given to the green solvent - ionic liquids. In this research, imidazolium ionic liquids were used to examine the recovery of 2,3-butanediol from fermentation broths. The influences of the temperature and concentration of 2,3-butanediol on phase formation were determined using two systems of 1-butyl-3-methylimidazolium chloride ([C(4)mim] [CI])-K2HPO4 and 1-ethyl-3-methylimidazolium trifluoromethanesulfonate ([C(2)mim)(CF3SO3])-K2HPO4 . The partition behaviors of 2,3-butandiol and ionic liquids, and the selectivity of 2,3-butanediol over glucose and organic acids were investigated and compared at different concentrations of ionic liquids and K2HPO4 . Most of 2,3-butanediol and ionic liquids were distributed to the top phase, whereas different trends of partition coefficient variation were observed. Under the condition of 25% [C(2)mim] [CF3SO3]-30% K2HPO4 (w/w), the recovery of 2,3-butanediol and [C(2)mim] [CF3SO3] was 95.7% and 99.5%, respectively, and selectivity for glucose, succinic acid and lactic acid was 2.59, 115 and 20.8, respectively.
引用
收藏
页码:175 / 181
页数:7
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