生物催化3-(4-氯苯基)-戊二腈去对称性水解合成光学纯巴氯芬的关键前体

研究了利用生物催化剂制备(S)-4-氰基-3-(4-氯苯基)-丁酸.以3-(4-氯苯基)-戊二腈为底物,采用苯酚-次氯酸钠法对实验室保藏的菌株进行筛选,得到一株产物立体选择性较高的菌株赤霉菌Gibberella intermedia WX12,并对其催化特性和发酵条件进行了初步研究.以30 g/L的乳糖和20 g/L的蛋白胨分别为碳、氮源,发酵培养96 h,收集的菌体在50 mmol/L磷酸缓冲液(pH 8.0)中30℃催化反应24 h,将3-(4-氯苯基)-戊二腈转化为4-氰基-3-(4-氯苯基)-丁酸,产率为90％.将产物化学转化为巴氯芬,手性HPLC分析表明水解产物构型是(S),其对映异构体过量值ee＞ 99％.该产物可以用来合成光学纯的(R)-和(S)-巴氯芬.     

Bacillus megaterium WZ009催化合成(R)-4-氯-3-羟基丁酸乙酯和(S)-3-羟基-γ-丁内酯

以外消旋4-氯-3-羟基丁酸乙酯为唯一C源的富集培养筛选得到一株菌株WZ009,经16S rDNA测序鉴定为巨大芽胞杆菌(Bacillus megaterium)。B.megaterium WZ009静息细胞可以立体选择性催化(S)-4-氯-3-羟基丁酸乙酯水解和脱氯反应得到光学纯的(R)-4-氯-3-羟基丁酸乙酯(e.e.≥99%)和(S)-3-羟基-γ-丁内酯(e.e.≥95%)。笔者对B.megaterium WZ009不对称催化反应影响因素(温度、pH、中和剂、底物浓度、时间进程以及细胞重复利用)进行优化研究,确定了该反应体系最优条件:底物浓度200 mmol/L,中和剂氨水,pH 7.2,40℃反应12 h,转化率达到50.6%,底物对映体过量值为99.6%。该生物催化合成(R)-4-氯-3-羟基丁酸乙酯和(S)-3-羟基-γ-丁内酯过程具有良好的工业化应用前景。     

疏水离子液体中生物不对称还原制备手性醇

针对近平滑假丝酵母全细胞不对称还原2-羟基苯乙酮制备光学纯(R)-苯基乙二醇反应中底物的质量浓度、产量及质量平衡低的问题,运用多相萃取生物转化的原理,比较不同非水介质对不对称还原反应效率的影响,构建具有良好生物相容性和高质量平衡的水/疏水离子液体1-丁基-3-乙基咪唑六氟磷酸盐([BEIM]PF6)双相反应体系。考察该体系下辅助底物种类、辅助底物用量、底物质量浓度、催化剂用量、离子液体比例、p H和反应温度对生物催化反应的影响,通过正交试验设计和响应面法优化不对称还原2-羟基苯乙酮的反应条件,在最优反应条件下,产物质量浓度、产率和质量平衡得率分别达到15.35 g/L、76.8%和84.3%,产物的对映消旋值(e.e.值)大于99.9%。     

高分子膜载体固定化酵母催化2-辛酮不对称还原

以戊二醛交联尼龙6膜载体固定化面包酵母DX213,采用固定化酵母细胞催化2-辛酮不对称还原得到(R)-2-辛醇。系统考察了有机溶剂、反应时间、pH、底物、辅助底物和热处理等因素对反应的产率和光学选择性的影响。结果表明,上述因素对酵母细胞催化不对称合成(R)-2-辛醇反应均有显著影响。二氯甲烷为该反应最适有机溶剂,在固定化细胞57 g/L(50℃预热50 min),水相与有机溶剂相体积比4/1,pH 7.0,初始2-辛酮浓度为60 mmoL/L(分别在反应0,10,17 h等分添加),蔗糖5.7 g/L和28℃条件下反应48 h,(R)-2-辛醇的产率和e.e.值分别达到89.3%和96.8%。     

酿酒酵母B5不对称还原制备手性药物中间体R-2′-氯-1-苯乙醇的研究

从11株微生物中筛选出4株具有不对称还原2′-氯-苯乙酮能力的酵母,其中酿酒酵母B5的还原产率与对映体选择性最佳。确定了酿酒酵母B5对2′-氯-苯乙酮还原的最佳反应时间为24h;最佳pH 8.0;最佳反应温度为25℃;最佳共底物为5%（体积比）乙醇。同时研究了底物浓度、微生物的量、微生物的培养条件等对反应产率和立体选择性的影响。细胞浓度为10.75mg/mL（细胞干重/反应体积）的酿酒酵母B5可将647mmol/L的2′-氯-苯乙酮100%地转化为R-2′-氯-1-苯乙醇,其对映体选择性为100%。酿酒酵母B5可重复利用的特点可提高产物的产量。     

酿酒酵母B5不对称还原制备手性药物中间体R-2′-氯-1-苯乙醇的研究

从 11株微生物中筛选出 4株具有不对称还原 2′ 氯 苯乙酮能力的酵母 ,其中酿酒酵母B5的还原产率与对映体选择性最佳。确定了酿酒酵母B5对 2′ 氯 苯乙酮还原的最佳反应时间为 2 4h ;最佳pH 8 0 ;最佳反应温度为2 5℃ ;最佳共底物为 5 % (体积比 )乙醇。同时研究了底物浓度、微生物的量、微生物的培养条件等对反应产率和立体选择性的影响。细胞浓度为 10 75mg mL(细胞干重 反应体积 )的酿酒酵母B5可将 6 47mmol L的 2′ 氯 苯乙酮10 0 %地转化为R 2′ 氯 1 苯乙醇 ,其对映体选择性为 10 0 %。酿酒酵母B5可重复利用的特点可提高产物的产量。     

羰基还原酶产生菌SW2026的产酶条件及其不对称催化还原4＇-氯苯乙酮

以4＇-氯苯乙酮为模型底物,对筛选得到的Candida krusei SW2026的羰基还原酶产酶条件进行研究。结果表明：适宜的发酵培养基组成为甘油50g/L,玉米浆20g／L,KH2PO4 4g／L,MgSO4·7H2O 1．5g／L;适宜的培养条件为温度30℃,初始pH6,摇床转速200r／min,发酵周期48h。在产酶发酵条件下培养的湿细胞对4＇-氯苯乙酮进行不对称还原反应,产物（S）-4＇-氯-α-苯乙醇的产率最高达88．56％,e．e．值稳定在87％左右。     

2-氧代-4-苯基丁酸乙酯还原酶产生菌筛选及产酶条件

研究了利用生物催化不对称还原的方法制备(R)-2-羟基-4-苯基丁酸乙酯[(R)-HPBE]。以2-氧代-4-苯基丁酸乙酯(OPBE)为底物,通过对实验室保藏菌株进行筛选,得到一株产物立体选择性较高的菌株G2ndida krusei SW2026,并对其发酵产酶条件进行研究。其最适的发酵培养基组成为4.5%葡萄糖,3%蛋白胨,1.5%牛肉膏,0.05%Mn~(2+);适宜的产酶发酵条件为初始pH 6.0,温度28℃,摇床转速180 r/min,发酵周期48 h。将此条件下发酵培养的菌体用于OPBE的不对称还原反应,产物(R)-HPBE的对映体过量值(e.e.)可达97.33%,产率最高达到72.54%。     

面包酵母催化不对称合成4-氯-(R)-3-羟基丁酸乙酯

以4 氯乙酰乙酸乙酯为原料,以面包酵母为手性生物催化剂,选择性合成光学活性4 氯 (R) 3 羟基丁酸乙酯。经IR、GC MS、1HNMR和旋光度测定,表明所得产品的结构与预期的结构一致。分别考察了面包酵母用量、葡萄糖浓度、底物投入量、pH值、反应时间以及反应温度等因素对产品比旋光度的影响。结果表明,4 氯乙酰乙酸乙酯不对称生物还原反应的适宜条件为:面包酵母6 0 0g/L、葡萄糖2 0g/L、反应温度34℃、底物加量16mL/L、反应时间4 8h、pH为5 ,产品的比旋光度为[α]2 0D = 13 9°。     

高产(+)γ-内酰胺酶菌株的筛选与发酵产酶研究

从土壤中筛选获得高产(+)γ-内酰胺酶的微生物菌株,并鉴定和保藏为Delftia sp.CGMCC No.5755.对该Delfiia sp菌株的发酵产酶条件进行了研究,结果表明,最适发酵培养基为:蔗糖30 g/L,蛋白胨30 g/L,牛肉膏25 g/L,乙酰胺5 g/L,MgS04 1 g/L;最适发酵温度及初始pH分别为32℃和pH 7.0.该菌株在上述条件下发酵培养20 h,菌体生物量为16.0 g/L,(+)γ-内酰胺酶的酶活为692 U/L.采用Delftia sp.静息细胞对100 g/L的外消旋底物2-氮杂二环-[2.2.1]-庚烷-5-烯-3-酮(简称(±)γ-内酰胺)的水解拆分反应中,产物(-)γ-内酰胺光学纯度大于99.9％e.e.,转化率为53.7％.研究为生物催化法高效制备光学纯(+)γ-内酰胺提供了可行的途径.     

（S）-（-）-β-羟基苯丙酸乙酯的微生物法合成

采用酿酒酵母CGMCC No．2266菌体,不对称还原β-羰基苯丙酸乙酯制备光学纯（S）-（-）-β-羟基苯丙酸乙酯。结果表明：采用初始pH为8．0的液体发酵培养基培养的CGMCCNo．2266菌体经过50℃预热处理30min后用于生物转化获得的（S）-（-）-G-羟基苯丙酸乙酯对映体过剩值可以达到100％ee。确定了合成（S）-（-）-β-羟基苯丙酸乙酯的较佳转化条件为pH7．0,温度30℃,转化时间24h,底物浓度为3．63mmol／L,菌体用量为86g/L（干重／反应体积）。以10％葡萄糖为辅助底物,产率比不加辅助底物时提高了75．4％。在最佳转化条件下反应转化率及（S）-（-）-β-羟基苯丙酸乙酯对映体过剩值可分别达到98．4％和100％ee。     

重组青霉素G酰化酶拆分制备（S）-邻氯苯甘氨酸

对产青霉素G酰化酶的重组枯草芽胞杆菌发酵产酶条件进行优化,确定优化后的发酵条件：可溶性淀粉10g/L、蛋白胨12g/L、酵母粉3g/L、NaCl10g,／L;pH7．5、培养温度37℃、装液量80mL（500mL三角瓶）、培养28h,青霉素G酰化酶的表达水平由最初的7．34U／mL提高至18．23U／mL。以表达青霉素G酰化酶的枯草芽胞杆菌发酵液为酶源,在水相中对映选择性催化N-苯乙酰-（R,S）-邻氯苯甘氨酸制备（S）-邻氯苯甘氨酸,当底物浓度为100mol／L时转化4h,转化率达44．2％。对底物浓度为80mmoL／L反应液中的（S）-邻氯苯甘氨酸进行分离,达到理论收率的94．29％（以N-苯乙酰-（R,S）-邻氯苯甘氨酸的0．5倍摩尔量为理论产率）,e．e．值大于99．9％。170℃条件下,N-苯乙酰-（R）-邻氯苯甘氨酸与苯乙酸共熔消旋为N-苯乙酰-（R,S）-邻氯苯甘氨酸可用于循环拆分。     

Highly enantioselective reduction of 4-(trimethylsilyl)-3-butyn-2-one to enantiopure (R)-4-(trimethylsilyl)-3-butyn-2-ol using a novel strain Acetobacter sp. CCTCC M209061

The biocatalytic reduction of 4-(trimethylsilyl)-3-butyn-2-one to enantiopure (R)-4-(trimethylsilyl)-3-butyn-2-ol was successfully conducted with high enantioselectivity using immobilized whole cells of a novel strain Acetobacter sp. CCTCC M209061, newly isolated from kefir. Compared with other microorganisms that were investigated, Acetobacter sp. CCTCC M209061 was shown to be more effective for the bioreduction reaction, and afforded much higher yield and product enantiomeric excess (e.e.). The optimal buffer pH, co-substrate concentration, reaction temperature, substrate concentration and shaking rate were 5.0, 130.6 mM, 30 °C, 6.0 mM and 180 r/min, respectively. Under the optimized conditions, the maximum yield and the product e.e. were 71% and >99%, respectively, which are much higher than those reported previously. Additionally, the established biocatalytic system proved to be efficient for the bioreduction of acetyltrimethylsilane to (R)-1-trimethylsilylethanol with excellent yield and product e.e. The immobilized cells manifested a good operational stability under the above reaction conditions since they retained 70% of their catalytic activity after ten cycles of use.     

毕赤酵母不对称合成阿托伐他汀中间体

阿托伐他汀可通过抑制HMG-CoA还原酶与底物的结合来抑制胆固醇的合成,而 (R)-3-羟基-5-邻苯二甲酰亚胺基戊酸乙酯是阿托伐他汀合成的重要中间体。通过对实验室保藏菌种进行筛选,得到一株巴氏毕赤酵母X-33可将5-邻苯二甲酰亚胺-3-氧代戊酸乙酯还原为 (R)-3-羟基-5-邻苯二甲酰亚胺基戊酸乙酯。在磷酸盐缓冲液体系中考察了初始底物浓度、反应时间、辅助底物、葡萄糖添加量、pH、温度等因素对产物收率和对映体选择性的影响,获得了较佳的反应条件。选择底物投料量为7 g/L时,当菌体浓度120 g/L,葡萄     

Efficient synthesis of enantiopure (S)-4-(trimethylsilyl)-3-butyn-2-ol via asymmetric reduction of 4-(trimethylsilyl)-3-butyn-2-one with immobilized Candida parapsilosis CCTCC M203011 cells

In this paper, we show the substrate 4-(trimethylsilyl)-3-butyn-2-one is unstable, and can be easily cleaved into a carbonyl alkyne and trimethylhydroxysilane in aqueous buffer with pH above 6.0. However, this problem could be effectively solved by lowering the buffer pH. Meanwhile, the efficient synthesis of enantiopure (S)-4-(trimethylsilyl)-3-butyn-2-ol, a key intermediate for preparing a 5-lipoxygenase inhibitor, has been successfully conducted through the asymmetric reduction of 4-(trimethylsilyl)-3-butyn-2-one with immobilized Candida parapsilosis CCTCC M203011 cells. For optimization of the reaction, various influential variables, such as buffer pH, co-substrate concentration, reaction temperature and substrate concentration, were systematically examined. All the factors mentioned above had effect on the reaction to some extent. The optimal buffer pH, co-substrate concentration, reaction temperature and substrate concentration were 5.0, 65.3 mM, 30 °C and 3.0 mM, respectively, under which the maximum yield and product e.e. were as high as 81.3% and >99.9% after a reaction time of 1 h, which are much higher than the corresponding values previously reported.     

Improved production of (R)-2-octanol via asymmetric reduction of 2-octanone with Oenococcus oeni CECT4730 in a biphasic system

Abstract

Oenococcus oeni CECT4730, which catalyses the asymmetric reduction of 2-octanone to (R)-2-octanol with high enantioselectivity, was further studied to exploit its potential for production of (R)-2-octanol in an aqueous/organic solvent biphasic system. Variables such as the volume ratio of aqueous to organic phase (V_a/V_o), buffer pH, reaction temperature, shaking speed, co-substrates and the ratio of biocatalyst to substrate were examined with respect to the molar conversion, the initial reaction rate and the product enantiomeric excess (e.e.). Under the optimized conditions (V_a/V_o=1:1 (v/v), buffer pH=8.0, reaction temperature=30°C, shaking speed=150 rev/min, ratio of glucose to biomass=5.4:l (w/w), ratio of biocatalyst to substrate=0.51:l (g/mol)), the highest space time yield of (R)-2-octanol, 24 mmol L^?1 per h, and >98% product e.e. were obtained at a substrate concentration close to 1.0 mol L^?1 after 24 h reduction.     

Efficient asymmetric reduction of 4-(trimethylsilyl)-3-butyn-2-one by Candida parapsilosis cells in an ionic liquid-containing system

Hydrophilic ionic liquids (ILs) were employed as green solvents to construct an IL-containing co-solvent system for improving the asymmetric reduction of 4-(trimethylsilyl)-3-butyn-2-one by immobilized Candida parapsilosis cells. Among 14 hydrophilic ILs examined, 1-(2'-hydroxyl)ethyl-3-methylimidazolium nitrate (C(2)OHMIM·NO(3)) was considered as the most suitable IL for the bioreduction with the fastest initial reaction rate, the highest yield and the highest product e.e., which may be due to the good biocompatibility with the cells. For a better understanding of the bioreduction performed in the C(2)OHMIM·NO(3)-containing co-solvent system, the effects of several crucial variables were systematically investigated. The optimal C(2)OHMIM·NO(3) content, substrate concentration, buffer pH, co-substrate concentration and temperature were 10% (v/v), 3.0 mmol/L, 5.0, 98.1 mmol/L and 30°C, respectively. Under the optimal conditions, the initial reaction rate, the maximum yield and the product e.e. were 17.3 μmol/h g(cell), 95.2% and >99.9%, respectively, which are much better than the corresponding results previously reported. Moreover, the immobilized cells remained more than 83% of their initial activity even after being used repeatedly for 10 batches in the C(2)OHMIM·NO(3)-containing system, exhibiting excellent operational stability.     

南海深海微生物酯酶EST12-7在制备(R)-2-氯丙酸乙酯中的应用研究

利用来源南海深海的微生物酯酶EST12-7不对称水解反应拆分制备（R）-2-氯丙酸乙酯。并探寻了温度、pH、底物浓度、有机溶剂和反应时间等因素对酯酶EST12-7催化制备（R）-2-氯丙酸乙酯的影响。结果表明,深海微生物酯酶EST12-7催化制备（R）-2-氯丙酸乙酯的最佳反应条件为：13.8 μg/ml酯酶EST12-7,50 mmol/L（±）-2-氯丙酸乙酯,2%正癸醇,pH8.5,30℃,0.05mol/L Tris-HCl,反应60 min。在最佳反应条件下,（±）-2-氯丙酸乙酯的转化率可达49%,所制备的（R）-2-氯丙酸乙酯的光学纯度为98%。通过对酯酶EST12-7拆分制备（R）-2-氯丙酸甲酯和（R）-2-氯丙酸乙酯进行比较,2-氯丙酸酯中的链长对酯酶EST12-7拆分反应有极大的影响。