羰基还原酶产生菌Candida ontarioensis制备(R)-2-氯-1-(3-氯苯基)乙醇

从实验室保藏的菌株中筛选获得Candida sp.PT2A,并通过18S rRNA鉴定为安大略假单胞菌Candida on-tarioensis。对C.ontarioensis不对称还原合成(R)-2-氯-1-(3-氯苯基)乙醇的发酵产酶条件和转化条件进行优化,确定了最适的发酵产酶条件和转化条件:温度30℃,初始pH 6.5,摇床转速180 r/min,菌体质量浓度200 g/L。采用2-氯-1-(3-氯苯基)乙酮质量浓度为10 g/L时,还原反应72 h,(R)-2-氯-1-(3-氯苯基)乙醇的e.e.值为99.9%,产率为99%;底物质量浓度提高至30 g/L时,产率下降为84.3%。采用十六烷基三甲基溴化铵(CTAB)对C.ontarioensis细胞进行通透性处理(CTAB g/L,4℃下处理20 min),在30 g/L底物下反应24 h,产物的e.e.和产率分别达到99.9%和97.5%。     

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.     

产环氧化物水解酶的黑曲霉菌种分离和发酵条件的研究

从土壤中筛选出一株能将苯基环氧乙烷立体选择性水解为R－苯基乙二醇的环氧化物水解酶的黑曲霉SQ－6。对其产酶发酵条件进行了研究,最佳碳,氮源分别为2．0％蔗糖和2．0％玉米浆,最适初始pH为4．0,该酶不需诱导,同时还研究了其他发酵条件对产酶的影响,使用含酶细胞进行底物苯基环氧乙烷转化。产物（R）－苯基乙二醇转化率为41％,ee值为99％。     

mRNA翻译起始区二级结构优化提高(R)-羰基还原酶的表达及催化效率

为了提高近平滑假丝酵母(Candida parapsilosis CCTCC M203011)的(R)-羰基还原酶在大肠杆菌中的表达水平及催化效率,对酶编码基因mRNA翻译起始区中+1～+78区进行二级结构的优化,并构建了相应的突变体。优化后mRNA翻译起始区的发夹结构明显减少,自由能显著下降(由原始的?9.5kcal/mol降至?5.0kcal/mol),使酶蛋白的表达水平及粗酶比活力分别比优化前提高了4～5倍和61.9%。在高底物浓度(5.0g/L2-羟基苯乙酮)下,优化突变株不对称转化效率较高,产物(R)-苯基乙二醇的光学纯度和产率分别为93.1%e.e.和81.8%,比优化前提高了27.5%和40.5%。研究结果表明:优化mRNA翻译起始区的二级结构,克服蛋白翻译启动的空间位阻,不仅能促进翻译的顺利进行,使目标蛋白得到高效表达,而且有利于蛋白空间结构的正确折叠,有效提高酶蛋白活力及生物催化功能。     

响应面法优化热带假丝酵母104菌株产羰基还原酶发酵培养基

通过菌种优选得到产高选择性羰基还原酶的热带假丝酵母(Candida tropicalis)104菌株,可不对称还原1-(3,5-二三氟甲基)苯基乙酮生成(S)-1-(3,5-二三氟甲基)苯基乙醇,对映体过量值>99.9%。采用部分因子实验设计考察发酵培养基中各组分对产酶的影响,结果表明,酵母粉、葡萄糖和NH4Cl浓度对产酶影响显著。继而采用最陡爬坡路径逼近最大响应区域,并结合中心组合实验和响应面对3个显著性因素进行分析,得到优化的发酵培养基组成:葡萄糖47.14g/L,酵母粉13.25g/L,NH4Cl2.71g/L,MgSO4·7H2O0.4g/L,KH2PO41g/L和K2HPO41g/L。采用该优化培养基,供试菌株的羰基还原酶活力达851.13U/L,较优化前提高了65.2%。     

酶法拆分手性化合物HPBE

R-HPBE(2-羟基4苯基丁酸乙酯)是一种重要的医药中间体,可以通过脂肪酶催化水解外消旋体得到。介绍了此催化过程的机理、工艺、产物检测等,并通过酶在疏水载体上的界面吸附对酶进行固定化,以提高酶活及对映选择性。     

产环氧化物水解酶的黑曲霉菌种分离和发酵条件的研究*

从土壤中筛选出一株能将苯基环氧乙烷立体选择性水解为R-苯基乙二醇的环氧化物水解酶的黑曲霉SQ-6。对其产酶发酵条件进行了研究,最佳碳、氮源分别为2.0%蔗糖和2.0%玉米浆,最适初始pH为4.0,该酶不需诱导,同时还研究了其他发酵条件对产酶的影响。使用含酶细胞进行底物苯基环氧乙烷转化,产物(R)-苯基乙二醇转化率为41%,ee值为99%。     

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%。     

利用短短芽孢杆菌进行酮还原酶CgKR2的高效表达与纯化

酮还原酶CgKR2能够一步还原前手性羰基化合物生成高附加值的手性醇,有望解决手性醇传统制备方法的步骤烦琐和高成本问题,具有很高的经济效益。研究表明,CgKR2催化底物2-氧代-4-苯基丁酸乙酯(OPBE)生成普利类降压药的重要中间体(R)-2-羟基-4-苯基丁酸乙酯[(R)-HPBE]具有良好效果。但CgKR2的生产成本高昂、过程烦琐。利用短短芽孢杆菌胞外分泌表达酮还原酶CgKR2,获得该酶的高效表达,并经简便的一步镍亲和层析纯化,即获得高纯度酮还原酶CgKR2,产率高达每升发酵7. 8mg纯酶。以酶标板法测定其比活力、温度稳定性以及动力学参数等基本酶学性质,结果显示,CgKR2的比活力为(78. 32±7. 62) U/mg、Km为(0. 2±0. 02) mmol/L、Vmax为(117. 64±3. 6)μmol/(min·mg)、Kcat为73s-1,与以往报道的数据一致,并且获得的CgKR2纯酶在30℃下孵育72h依然保持80%的活性,酶活的稳定性远好于以往的制备方法。开发出的一套简便高效的酮还原酶CgKR2表达纯化工艺,降低了生产成本、简化了生产工艺,可推进手性醇生物催化制备的普及,对其他生物催化工程酶的制备方法研究也有借鉴作用。     

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。     

Scalable biocatalytic synthesis of optically pure ethyl (R)-2-hydroxy-4-phenylbutyrate using a recombinant E. coli with high catalyst yield

Ethyl (R)-2-hydroxy-4-phenylbutanoate [(R)-HPBE] is a versatile and important chiral intermediate for the synthesis of angiotensin-converting enzyme (ACE) inhibitors. Recombinant E. coli strain coexpressing a novel NADPH-dependent carbonyl reductase gene iolS and glucose dehydrogenase gene gdh from Bacillus subtilis showed excellent catalytic activity in (R)-HPBE production by asymmetric reduction. IolS exhibited high stereoselectivity (>98.5% ee) toward α-ketoesters substrates, whereas fluctuant ee values (53.2–99.5%) for β-ketoesters with different halogen substitution groups. Strategies including aqueous/organic biphasic system and substrate fed-batch were adopted to improve the biocatalytic process. In a 1-L aqueous/octanol biphasic reaction system, (R)-HPBE was produced in 99.5% ee with an exceptional catalyst yield (gproduct/gcatalyst) of 31.7 via bioreduction of ethyl 2-oxo-4-phenylbutyrate (OPBE) at 330 g/L.     

Biocatalytic synthesis of ethyl (R)-2-hydroxy-4-phenylbutyrate with Candida krusei SW2026: A practical process for high enantiopurity and product titer

Ethyl (R)-2-hydroxy-4-phenylbutyrate ((R)-HPBE), a key intermediate in the production of angiotensin-converting enzyme (ACE) inhibitors, was prepared by the microbial reduction of ethyl 2-oxo-4-phenylbutyrate (OPBE). Among 63 microorganisms tested, Candida krusei SW2026, for the first time, was proven to be a highly effective biocatalyst in this reduction process, leading to the (R)-enantiomer in 99.7% ee and 95.1% yield at 2.5 g/L of OPBE (under optimal conditions of 30 °C, pH 6.6, and in the presence of 5% glucose as co-substrate). In order to achieve higher product concentration with desired enantiopurity and yield for application in large-scale production, strategies such as substrate fed-batch and aqueous/organic biphasic system were successfully conducted in the biotransformation reaction. At 20 g/L of OPBE, the enantiomeric excess (ee), yield, and product concentration were enhanced to 97.4%, 82.0%, and 16.6 g/L, respectively, in water/dibutyl phthalate biphasic system, compared with 87.5%, 45.8%, and 9.2 g/L in aqueous medium. This study provides an attractive process of (R)-HPBE production for potential green chemistry applications.     

Improved production of ethyl-(R)-2-hydroxy-4-phenylbutyrate with pretreated Saccharomyces cerevisiae in water/organic solvent two-liquid phase systems

Baker's yeast pretreated with α-phenacyl chloride was employed to improve the enantioselectivity of the asymmetric reduction of ethyl-2-oxo-4-phenylbutyrate (EOPB) to ethyl-(R)-2-hydroxy-4-phenylbutyrate ((R)-EHPB) and maintain a high activity of the yeast. A water/organic solvent two-liquid phase system was also introduced to overcome the strong substrate and product inhibition of the enzyme; the highest catalytic activity and enantioselectivity were obtained in a water/benzene two-liquid phase system. When the reduction was catalyzed with pretreated yeast (300 mg mL^?1 buffer) in the water/benzene two-liquid phase system (V_aq/V_ben=20:40), 41.9% molar conversion of EOPB and 87.5% e.e. of (R)-EHPB were obtained in 48 h, using pH 8.0 phosphate buffer with 1.5% (v/v) of ethanol added as a co-substrate at 30°C, even with an initial EOPB concentration of 400 mM and a final EHPB concentration as high as 167.7 mM.     

Effect of ionic liquid [BMIM][PF<Subscript>6</Subscript>] on asymmetric reduction of ethyl 2-oxo-4-phenylbutyrate by <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>

The effect of ionic liquid 1-butyl-3-methylimidazolium hexafluorophosphate ([BMIM][PF₆]) on the asymmetric reduction of ethyl 2-oxo-4-phenylbutyrate (EOPB) to synthesize optical active ethyl 2-hydroxy-4-phenylbutyrate (EHPB) catalyzed by Saccharomyces cerevisiae was investigated. (R)-EHPB [70.4%, e.e.(R)] is obtained using ethyl ether or benzene as the solvent. The main product is (S)-EHPB [27.7%, e.e.(S)] in [BMIM][PF₆]. However, in ionic liquid-water (10:1, v/v) biphasic system, the enantioselectivity of the reduction is shifted towards (R)-side, and e.e.(R) is increased from 6.6 to 82.5% with the addition of ethanol (1%, v/v). The effect of the use of [BMIM][PF₆] as an additive in relatively small amounts on the reduction was also studied. We find that there is a decline in the enantioselectivity of the reduction in benzene. In addition, a decrease in the conversion of EOPB and the yield of EHPB with increasing [BMIM][PF₆] concentrations occurs in either organic solvent–water biphasic systems or benzene.     

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     

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。     

One‐pot synthesis of (R)‐1‐(pyridin‐4‐yl)ethyl acetate using tandem catalyst prepared by co‐immobilization of palladium and lipase on mesoporous foam: Optimization and kinetic modeling

The synthesis of (R )‐1‐(pyridin‐4‐yl)ethyl acetate was achieved over tandem palladium‐lipase catalyst with 100% selectivity using 4‐acetyl pyridine as a reactant. The 2% w /w palladium and lipase catalyst was successfully co‐immobilized in the microenvironment of the mesocellular foam and characterized by various techniques. The palladium metal from catalyst hydrogenated 4‐acetyl pyridine to form 1‐(pyridin‐4‐yl)ethanol. The generated intermediate product then underwent kinetic resolution over lipase and selectively gave (R )‐1‐(pyridin‐4‐ yl)ethyl acetate. The catalytic conditions were then studied for optimal performance of both steps. The reaction conditions were optimized to 50 °C and toluene as a solvent. Both chemical and enzymatic kinetic models of the reaction were developed for a given set of reaction conditions and kinetic parameters were predicted. At optimal conditions, the obtained selectivity of intermediate (1‐(pyridin‐4‐yl)ethanol) was 51.38%. The final product yield of ((R )‐1‐(pyridin‐4‐yl)ethyl acetate) was 48.62%.     

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%。