摘要
在邻苯二甲酸二丁酯中采用固定化酿酒酵母CGMCC No.2266不对称还原β-羰基苯丙酸乙酯制备(S)-(-)β--羟基苯丙酸乙酯。将干重为430 mg的100 ml菌液50℃预热处理30 min,以2%海藻酸钠固定化得到的直径为2 mm的固定化细胞增殖培养72 h,在300 ml邻苯二甲酸二丁酯中转化17.2 mmol.L-1β-羰基苯丙酸乙酯,摩尔产率和对映体过剩值可以分别达到92.2%和100%。固定化细胞可以较好地重复利用于转化反应10次。产率随底物浓度的增高而降低,分批加入底物可以降低底物浓度过高对反应过程的抑制。
(S) - (--) -β-hydroxy benzenepropanoic acid ethyl ester was synthesized by asymmetric reduction of β-carbonyl phenylpropionate with immobilized CGMCC No. 2266 in dibutyl phthalate. 100 ml microbial liquor containing 430 mg (dry weight) biomass preheated at 50℃ for 30 rain was immobilized. After re culturing for 72 h, the immobilized cells of 2 mm diameter prepared by 2% sodium alginate was used to reduce 17.2 mmol · L ^-1 β-carbonyl phenylpropionate in 300 ml dibutyl phthalate. The yield and enantiomeric excess of (S) - (--) -β hydroxy benzenepropanoic acid ethyl ester reached 92.20/00 and 100% respectively. Immobilized CGMCC No. 2266 can be reused in reaction for ten times. The yield decreased with increasing substrate concentration. Batch addition of substrate can reduce inhibition of high concentration substrate.
出处
《化工学报》
EI
CAS
CSCD
北大核心
2009年第2期421-427,共7页
CIESC Journal
基金
浙江省科技计划项目(2007C33047)~~