采用通透性处理的安大略假丝酵母全细胞高效合成(R)-2-氯-1-(3-氯苯基)乙醇(英文)

考察了利用安大略假丝酵母(Candida ontarioensis)静息细胞不对称催化2-氯-1-(3-氯苯基)乙酮合成(R)-2-氯-1-(3-氯苯基)乙醇的转化反应条件.结果表明,当底物浓度为10g/L时,在最适转化条件下反应72h,产物的ee值和产率分别达到99.9%和99.0%.采用4g/L十六烷基三甲基溴化铵对Candida ontarioensis细胞于4℃通透性处理20min后,全细胞的酶活提高2倍以上.当底物浓度提高为30g/L,转化24h后,产物的ee和产率分别达到99.9%和97.5%.该研究为高效制备(R)-2-氯-1-(3-氯苯基)乙醇提供了可行途径,并为生物催化合成芳基手性醇类手性中间体提供了理论指导。     

有机溶剂/缓冲液双相体系中固定化Acetobacter sp.CCTCC M209061细胞催化1-(4-甲氧基)-苯基乙醇不对称氧化反应

在有机溶剂/缓冲液双相体系中, 利用固定化醋酸杆菌Acetobacter sp.CCTCC M209061细胞高对映体选择性地催化1-(4-甲氧基)-苯基乙醇(MOPE)的不对称氧化反应, 成功地拆分外消旋MOPE得到对映体纯(S)-MOPE. 与游离细胞相比, 固定化细胞催化反应速度有所降低, 但其稳定性(包括操作稳定性、 热稳定性和储藏稳定性)明显提高. 固定化细胞连续使用10批次(每批次12 h)后, 仍能保留其初始催化活性的58%以上, 而游离细胞仅保留约20%的相对活性. 在所考察的不同有机溶剂中, 正己烷不仅能较好地溶解底物, 而且对细胞的生物相容性相对较好, 因而提高了反应底物浓度、 反应初速度、 对映体回收率及残留底物e.e.值, 是反应体系中最适宜的有机相. 该反应的最适宜正己烷体积分数为60%, 辅底物为50 mmol/L丙酮, 底物浓度为40 mmol/L, 缓冲液pH=6.5, 反应温度为30 ℃; 在此条件下, 反应初速度为80.4 μmol/min, 反应12 h后, 对映体回收率和残留底物e.e.值分别为51.0%和99.9%, 明显好于水单相反应体系.     

近平滑假丝酵母细胞催化乙酰基三甲基硅烷不对称还原反应

 采用近平滑假丝酵母细胞用于催化乙酰基三甲基硅烷不对称还原反应, 可高选择性地生成 (R)-1-三甲基硅乙醇. 结果表明, 固定化于海藻酸钙的细胞催化该反应的产物收率比游离细胞的高. 不同辅底物对该反应的影响显著, 以葡萄糖为辅底物时, 反应的初速率较快, 产物收率较高. 该反应的最适条件为: 辅底物 (葡萄糖) 浓度 110 mmol/L, 振荡速度 180 r/min, 缓冲液 pH 值 6.0, 反应温度 30 oC, 底物浓度 20 mmol/L. 在此反应条件下反应的初速率、产物收率和产物的 ee 值分别为 11.4 μmol/h, 96.5% 和 99.9%.     

羰基还原酶CR2重组酶体系不对称合成(S)-N,N-二甲基-3-羟基-3-(2-噻吩)-1-丙胺

构建了羰基还原酶CR2重组酶体系,并优化了相关的酶促催化反应条件.通过在催化体系中添加辅酶NADP+(0.1 mmol/L)和辅底物葡萄糖(120 g/L),在30℃及p H=8.0的条件下反应4 h,CR2重组酶体系不对称还原N,N-二甲基-3-酮-3-(2-噻吩)-1-丙胺(DKTP,10 g/L),合成了高光学纯度(S)-N,N-二甲基-3-羟基-3-(2-噻吩)-1-丙胺[(S)-DHTP,e.e.值99.9%],产率为62%.在酶促催化过程中,由于辅酶循环生成葡萄糖酸导致反应体系p H值下降而影响催化效率.通过调控反应体系p H值,(S)-DHTP的产率提高到68%.不同浓度底物的反应过程表明底物对CR2酶促反应具有抑制作用,且在10 g/L底物浓度下反应的时空产率可达1.3 g·L-1·h-1.     

有机溶剂/缓冲液双相体系中绿豆环氧化物水解酶催化环氧苯乙烯不对称水解反应

研究了有机溶剂/缓冲液双相体系中绿豆环氧化物水解酶高立体选择性地催化外消旋环氧苯乙烯水解生成(R)-苯基乙二醇反应.结果表明,与单水相反应体系相比,有机溶剂/缓冲液双相反应体系不仅有效地抑制环氧苯乙烯的非酶水解反应,而且明显提高底物的浓度,产物的收率和ee值更高.在所考察的不同有机溶剂中,正己烷不仅能较好地溶解底物,而...     

嗜热古细菌Sulfolobus tokodaii脱卤酶在D-乳酸生产中的应用

将来源于嗜热古菌Sulfolobus tokodaii的脱卤酶(L-HADST)基因克隆到载体p ET28b,转化大肠杆菌BL21(DE3)进行表达,在蛋白的N末端带有6个组氨酸融合标签,纯化后经聚丙烯酰胺凝胶电泳显示融合蛋白的分子量约为25000.融合蛋白催化2-氯丙酸(2-CPA)的最适反应温度为70℃,最适p H值为9.5.以外消旋2-CPA为底物生产D-乳酸,利用HPLC检测反应液中2-CPA及乳酸的变化,发现L-HADST只催化L-2-CPA脱氯反应.对酶催化反应条件进行了优化,结果表明,在p H值为9.5,温度为60℃的条件下,当反应体系中缓冲液浓度为3 mol/L,底物浓度为0.5 mol/L,酶浓度为3×104U/L时有较高的底物转化率及乳酸生成量.依据条件优化结果可知,影响反应速度的因素有底物浓度、缓冲液浓度以及酶浓度,其中底物浓度变化对转换率的影响最明显.     

手性环氧氯丙烷的CPO酶催化不对称合成

基于氯过氧化物酶(CPO)对有机底物的手性识别,以CPO催化、叔丁基过氧化氢(TBHP)氧化3-氯丙烯合成手性(R)-环氧氯丙烷,并引入多羟基化合物为添加剂提高了目标产物的产率及对映选择性.反应主要受体系的pH值以及CPO用量等因素控制.UV-vis及CD光谱分析表明,反应体系中引入多羟基化合物(甘油、PEG400、PEG600)时,CPO的血红素辅基暴露程度增加,底物容易接近活性中心,同时CPO的α-螺旋结构得以加强,从而有效提高了产物收率.CPO对底物的手性识别主要基于底物与酶催化中间体([Fe(IV)=O·]+)形成的复合物对酶的稳定性的影响.通过反应条件优化,(R)-环氧氯丙烷产率可达67.3%,对映选择性(ee)97.5%.     

羰基还原酶突变体高选择性催化不对称还原大位阻羰基化合物

以立体选择性羰基还原酶(RCR)的双突变酶RCR-F285A/W286A为对象,考察了该突变酶对酮酯类和杂环酮类底物的催化性能(包括酶活力和动力学参数)及对映体选择性,发现其对2-氧代-4-苯基丁酸乙酯(OPBE)、苯甲酰基乙酸乙酯(EBA)和1-苄基-3-吡咯烷酮均具有酶活性,并且以高光学纯度生成相应手性醇(e.e.99%).考察了反应条件对产率最高的OPBE的不对称转化反应的影响,结果表明,当pH=7. 0,反应温度30℃,3. 5%(体积分数)的异丙醇作助溶剂,加入1 g/L底物时,产率达到80. 3%.进一步通过分批补料减弱底物抑制作用,在10 g/L的底物浓度下,时空产率为0. 062 g·L~(-1)·h~(-1),为酶法不对称合成(R)-2-羟基-4-苯基丁酸乙酯[(R)-HPBE]的工业应用提供了实验基础.     

CTAB透性化酵母细胞生物催化合成(S)-(+)-3-羟基丁酸乙酯

 利用十六烷基三甲基溴化铵(CTAB)透性化啤酒酵母细胞中高活性的脱氢酶,借助于辅助底物乙醇和葡萄糖,对3-羰基丁酸乙酯(EOB)不对称还原合成(S)-(+)-3-羟基丁酸乙酯((S)-(+)-3-EHB)进行了研究. 结果表明,CTAB透性化酵母细胞中的醇脱氢酶和6-磷酸葡萄糖脱氢酶的活性分别比未经处理的酵母细胞高482倍和6.5倍. 在相同条件下,CTAB透性化细胞对EOB的还原比未经处理的酵母细胞快. 细胞浓度对反应有明显影响,当透性化酵母细胞浓度＜90 mg/ml时,(S)-(+)-3-EHB的产率和对映体过量值都较低; 当酵母细胞浓度≥90 mg/ml,在最佳进料速率、最适温度和pH条件下,振摇速度为125 r/min时, (S)-(+)-3-EHB的浓度达到最大值314 mmol/L. 在反应开始的6 h内,(S)-(+)-3-EHB的产率可达94%,对映体过量值≥98%,但24 h后产率和对映体过量值分别降低到85%和91%.     

高压CO2条件下粗状假丝酵母催化苯乙酮不对称还原合成α-苯乙醇

 研究了在高压CO2条件下利用粗状假丝酵母Candida valida CICC1444活性细胞催化苯乙酮不对称还原合成(R)-α-苯乙醇. 高压CO2条件可对粗状假丝酵母细胞的活性产生一定的影响,但反应的选择性反而有所提高,证实了高压CO2作为该反应环境是可行的. 考察了底物浓度、细胞用量、反应温度和压力等因素对反应的影响. 结果表明,这些因素对反应产率有很大的影响,在最佳反应条件下,反应底物苯乙酮的转化率和产物α-苯乙醇的产率均可达90%以上,对映体过量值(ee)保持在80%左右. 与常压静置条件下的反应相比,高压CO2条件下粗状假丝酵母催化苯乙酮不对称还原反应的转化率和产率分别提高了20%和40%左右,对映体选择性也提高了5%～10%.     

有机溶剂-水双液相体系脂肪酶不对称水解合成S-(+)-萘普生

采用有机溶剂－水双液相体系作为反应介质，并用键合有—Ｃ６Ｈ５的无定型多孔硅胶作为分散剂增大两相间的接触面，用圆柱状假丝酵母脂肪酶对萘普生甲酯进行不对称水解．考察了酶浓度、体系ｐＨ值、温度、分散剂对反应的影响．当转化率为２４．３％时，产品萘普生的对映体过量值（ｅｅ）为９４．９％，剩余底物萘普生甲酯的对映体过量值（ｅｅ）为３０．５％，当以异辛烷作为有机相时，该体系酶催化水解的对映体比率（Ｅ）约为５０．     

水/有机溶剂双相体系中色氨酸合成酶酶法合成L-色氨酸

在水/有机溶剂双相体系中,利用重组大肠杆菌DM206 [pET28a-trpBA/BL21 (DE3)]色氨酸合成酶催化L-丝氨酸和吲哚合成了L-色氨酸.考察了有机溶剂、有机相乙酸乙酯体积分数、反应温度、水相pH、底物L-丝氨酸与吲哚摩尔比、底物L-丝氨酸浓度、表面活性剂和酶添加量对色氨酸合成酶酶活的影响.结果表明,酶...     

离子液体中固定化光合细菌催化不对称还原反应的研究

采用苯乙酮为模式底物,选用了3种典型的离子液体作为反应介质系统研究了离子液体与缓冲液构成的均相及两相体系中固定化光合细菌催化不对称还原反应的特性．通过对构建的离子液体反应体系进行条件优化,发现与水相及有机相相比,离子液体作为生物催化反应介质更有利于还原反应的进行,并且离子液体及固定化细胞易回收重复利用．研究结果表明,在...     

Process Development through Solvent Engineering in the Biocatalytic Synthesis of the Heterocyclic Bulk Chemical ε‐Caprolactone

For an alternative synthetic approach toward the heterocyclic industrial chemical ε‐caprolactone, which is based on a biocatalytic oxidation of readily available cyclohexanol with air in aqueous media (using an alcohol dehydrogenase and a Baeyer–Villiger monooxygenase as enzyme components), a solvent engineering has been carried out identifying isooctane as a suitable co‐solvent. Biotransformations in an aqueous‐isooctane biphasic solvent system were found to proceed faster at both investigated substrate concentrations of 40 and 80 mm , respectively, compared with the analogous enzymatic reactions in pure aqueous medium. In addition, in all cases quantitative conversions were observed after a reaction time of 23 h when using isolated enzymes. The achievements indicate a high compatibility of isooctane [10%(v/v)] with the enzymes as well as the potential for an in situ removal of the organic reaction components, thus decreasing inhibition and/or destabilization effects of these organic components on the enzymes used. In contrast, so far, the use of recombinant whole‐cells gave less satisfactory results, which might be due to limitations of the permeation of, for example, the substrate through the cell membrane.     

Catalytic epoxidation of styrene–butadiene triblock copolymer with hydrogen peroxide

Styrene-butadiene-styrene linear block copolymer (SBS) can be epoxidized with hydrogen peroxide in the presence of methyltrioctylammonium tetrakis (diperoxotungsto) phosphate(3-) as the catalyst in a biphasic system. The effects of reaction time, temperature, solvent, the ratio of the organic phase to the aqueous phase, the concentration of the catalyst, hydrogen peroxide and polymer, respectively, are studied on the conversion of double bonds to oxirane groups. ¹H-NMR analysis confirms the absence of ring opening side reaction in this epoxidation reaction system up to at least 70% conversion of the double bonds. When the conversion of double bonds is over about 70% the resultant polymer is insoluble in chloroform even at reflux but soluble in polar solvents such as DMSO when heated. Toluene is a better solvent for the reaction than dichloroethane. The reaction rate constants are measured at four temperatures and the activation energy for the reaction with toluene as solvent is determined as 49.9 kJ/mol.     

Enzymatic Enantioselective Synthesis of （R）－2－Trimethylsilyl－2－hydroxyl－propionitrile by Defatted Apple Seed Meal

IntroductionOverthepastyears ,thesynthesisofchiralaldehyde cyanohydrinswaswellstudied .1Incontrasttochiralalde hyde cyanohydrins ,therewereonlyfewreportsaboutthepreparationofopticallyactiveketone cyanohydrins ,2 whichareusefulstartingmaterialsandintermediatesforthesyn thesisofmanychiralnaturalproducts .3Wethereforefo cusedonthepreparationofopticallyactivesiliconcontain ing (R ) ketone cyanohydrin ((R ) 2 trimethylsilyl 2 hy droxyl propionitrile)usingacetonecyanohydrinastran scyanationagen…     

A parametric study on biphasic medium conditions for the enantioselective production of naproxen by <Emphasis Type="Italic">Candida rugosa</Emphasis> lipase

A parametric study to increase the enantioselectivity of Candida rugosa lipase (CRL) toward S-Naproxen production by the hydrolysis of racemic Naproxen methyl ester in an aqueous-organic biphasic batch system was carried out. Effects of organic solvent type, aqueous phase/organic solvent volume ratio, agitation rate, concentrations of the substrate and the enzyme, pH of the aqueous phase, and temperature on the en antiomeric excess for the product (ee_p), on the enantiomeric ratio (E) and on the conversion (x) were evaluated. Employing isooctane as the solvent resulted in higher ee_p, E, and x than those obtained in hexane, cyclohexane, and toluene. The higher the volume ratio of aqueous phase/organic solvent employed, the higher the conversion and enantioselectivity achieved. The increase in agitation rate increased the hydrolysis rate. Higher concentration of racemic Naproxen methyl ester than 10 mg/mL decreased both the conversion and enantioselectivity. The increase in crude CRL concentration resulted in enhancement of x, but the decrease of fee_p and E. Acidic pH led to higher conversion and enantioselectivity than the medium and alkaline pH values. A further increase in temperature to over 45°C decreased the conversion and enantioselectivity. The highest enantiomeric ratio achieved in the S-Naproxen production was E=171.1, with x=49.8% and ee_p=95.7%.     

Separation of phenylsuccinic acid enantiomers using biphasic chiral recognition high‐speed countercurrent chromatography

High‐speed countercurrent chromatography (HSCCC) combined with biphasic chiral recognition was successfully applied to the resolution of phenylsuccinic acid enantiomers. d ‐Isobutyl tartrate and hydroxypropyl‐β‐cyclodextrin were employed as lipophilic and hydrophilic selectors dissolved in the organic stationary phase and aqueous mobile phase, respectively. The two‐phase solvent system was made up of n‐hexane/methyl tert‐butyl ether/water (0.5:1.5:2, v/v/v). Impacts of the type and concentration of chiral selectors, the pH value of the aqueous phase solution as well as the temperature on the separation efficiency were investigated. By means of preparative HSCCC, pure enantiomer was obtained by separating 810 mg of racemate with a purity >99.5% and a recovery rate between 82 and 85%. The experimental results indicate that biphasic recognition HSCCC provide a promising means for efficient separation of racemates.