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1.
面包酵母催化羰基不对称还原合成手性醇的研究   总被引:6,自引:0,他引:6  
以2-辛酮和4-氯乙酰乙酸乙酯(COBE)为模型底物分别考察了酵母细胞对直链甲基酮和陆羰基酯中的羰基不对称还原情况。实验发现不对称还原2-辛酮的产物主要是S型的2-辛醇,且对映体选择性很高。不对称还原COBE生成的主要是S(D)-型产物,反应COBE的转化率、光学选择性都比较高。同时发现COBE的浓度和产物对不对称还原都有一定负面的影响。  相似文献   

2.
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%。  相似文献   

3.
研究了固定化啤酒酵母细胞催化三甲基硅乙酮不对称还原反应,系统探讨了振荡速度、底物浓度、固定化细胞浓度、pH值和反应温度对反应速度、产率和产物光学纯度的影响。结果表明,上述因素对固定化啤酒酵母细胞催化三甲基硅乙酮不对称还原反应均有较显著的影响。振荡速度以150r/min为宜,底物浓度和固定化细胞浓度分别为14mmol/L和0.15g/mL较佳,适宜的pH值为7.3,最佳反应温度为25℃~30℃。在该优化反应条件下,反应最大产率和产物的光学纯度分别高达84.9%和90.2%ee。  相似文献   

4.
以戊二醛为交联剂,将壳聚糖球交联引入醛基,然后将交联的壳聚糖球浸泡在酵母细胞悬浮液中,制备了固定化酵母细胞壳聚糖球。以苯乙酮酸为底物,催化合成了D-扁桃酸。最优固定化条件是戊二醛的质量分数w(GA)=1%,酵母细胞与交联壳聚糖球的质量比m(Y):m(CB)0=0.5,交联时间为6h,固定化时间为18h,底物浓度为10mmol/L,在此条件下反应最大转化率和产物光学纯度分别高达67.86%和98.05?。固定化酵母壳聚糖球具有良好的重复使用性和贮存稳定性。  相似文献   

5.
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。  相似文献   

6.
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。  相似文献   

7.
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%。  相似文献   

8.
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。  相似文献   

9.
从实验室保藏的菌株中,筛选到一株立体选择性较高的产4-氯乙酰乙酸乙酯(COBE)羰基还原酶的菌株———出芽短梗霉(Aureobasidiumpullulans)SW0202,菌体产酶条件研究表明,最佳的发酵培养基配方为:麦芽糖30.0g/L,酵母膏20.0g/L,蛋白胨3.0g/L,(NH4)2SO45.0g/L,KH2PO42.0g/L,MgSO4.7H2O0.7g/L,最适发酵温度及初始pH分别为:28°C和pH6.0。该菌在此条件下发酵培养24h,产菌丝体生物量16.78g干菌体/L,COBE羰基还原酶酶活力达到1007U/L。在COBE的转化反应中,产物S-CHBE的浓度达到10.12g/L,光学纯度>97%e.e.。  相似文献   

10.
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%。  相似文献   

11.
A novel NADPH-dependent reductase (CaCR) from Candida albicans was cloned for the first time. It catalyzed asymmetric reduction to produce ethyl (S)-4-chloro-3-hydroxybutanoate ((S)-CHBE). It contained an open reading frame of 843 bp encoding 281 amino acids. When co-expressed with a glucose dehydrogenase in Escherichia coli, recombinant CaCR exhibited an activity of 5.7 U/mg with ethyl 4-chloro-3-oxobutanoate (COBE) as substrate. In the biocatalysis of COBE to (S)-CHBE, 1320 mM (S)-CHBE was obtained without extra NADP+/NADPH in a water/butyl acetate system, and the optical purity of the (S)-isomer was higher than 99% enantiomeric excess.  相似文献   

12.
An NADPH-dependent carbonyl reductase (PsCR) gene from Pichia stipitis was cloned. It contains an open reading frame of 849 bp encoding 283 amino acids whose sequence had less than 60% identity to known reductases that produce ethyl (S)-4-chloro-3-hydroxybutanoates (S-CHBE). When expressed in Escherichia coli, the recombinant PsCR exhibited an activity of 27 U/mg using ethyl 4-chloro-3-oxobutanoate (COBE) as a substrate. Reduction of COBE to (S)-CHBE by transformants in an aqueous mono-phase system for 18 h, gave a molar yield of 94% and an optical purity of the (S)-isomer of more than 99% enantiomeric excess.  相似文献   

13.
Ethyl(R)-4-chloro-3-hydroxybutanoate ((R)-CHBE) are obtained by cetyltrimetylammonium bromide (CTAB) permeabilized fresh brewer’s yeast whole cells bioconversion of ethyl 4-chloro-3-oxobutanoate (COBE ) in the presence of allyl bromide. The results showed that the activities of alcohol dehydrogenase (ADH) and glucose-6-phosphate dehydrogenase (G6PDH) in CTAB permeabilized brewer’s yeast cells increased 525 and 7.9-fold, respectively, compared with that in the nonpermeabilized cells and had high enantioselectivity to convert COBE to (R)-CHBE. As one of co-substrates, glucose-6-phosphate was preprepared using glucose phosphorylation by hexokinase-catalyzed of CTAB permeabilized brewer’s yeast cells. In a two phase reaction system with n-butyl acetate as organic solvent and with 2-propanol and glucose-6-phosphate as co-substrates, the highest (R)-CHBE concentration of 447 mM was obtained with 110–130 g/l of the CTAB permeabilized cells at optimized pH, temperature, feeding rate and the shake speed of 125 r/min. The yield and enantiomeric excess (ee) of (R)-CHBE reached 99.5 and 99%, respectively, within 6 h.  相似文献   

14.
An NADPH-dependent sorbose reductase from Candida albicans was identified to catalyze the asymmetric reduction of ethyl 4-chloro-3-oxobutanoate (COBE). The activity of the recombinant enzyme toward COBE was 6.2 U/mg. The asymmetric reduction of COBE was performed with two coexisting recombinant Escherichia coli strains, in which the recombinant E. coli expressing glucose dehydrogenase was used as an NADPH regenerator. An optical purity of 99% (e.e.) and a maximum yield of 1240 mM (S)-4-chloro-3-hydroxybutanoate were obtained under an optimal biomass ratio of 1:2. A highest turnover number of 53,900 was achieved without adding extra NADP+/NADPH compared with those known COBE-catalytic systems.  相似文献   

15.
Zygosaccharomyces rouxii catalysed the reduction of ethyl 4-chloroacetoacetate (ethyl 4-chloro-3-oxobutanoate) to the corresponding (S)-hydroxy ester (ethyl (S)-4-chloro-3-hydroxybutanoate) in high enantiomeric excess. The productivity of non-immobilised cells was compared to cells immobilised on a range of organic and inorganic supports. Cells immobilised in calcium alginate displayed a catalytic activity significantly higher than that of non-immobilised cells. A time dependent fall in the enantiomeric purity of the product was observed with the use of this matrix. This phenomenon was not seen in the reduction catalysed by non-immobilised cells.  相似文献   

16.
The asymmetric reduction of ethyl 4-chloro-3-oxobutanoate (COBE) to ethyl (S)-4-chloro-3-hydroxybutanoate ((S)-CHBE) was investigated. Escherichia coli cells expressing both the carbonyl reductase (S1) gene from Candida magnoliae and the glucose dehydrogenase (GDH) gene from Bacillus megaterium were used as the catalyst. In an organic-solvent-water two-phase system, (S)-CHBE formed in the organic phase amounted to 2.58 M (430 g/l), the molar yield being 85%. E. coli transformant cells coproducing S1 and GDH accumulated 1.25 M (208 g/l) (S)-CHBE in an aqueous monophase system by continuously feeding on COBE, which is unstable in an aqueous solution. In this case, the calculated turnover of NADP+ (the oxidized form of nicotinamide adenine dinucleotide phosphate) to CHBE was 21,600 mol/mol. The optical purity of the (S)-CHBE formed was 100% enantiomeric excess in both systems. The aqueous system used for the reduction reaction involving E. coli HB101 cells carrying a plasmid containing the S1 and GDH genes as a catalyst is simple. Furthermore, the system does not require the addition of commercially available GDH or an organic solvent. Therefore this system is highly advantageous for the practical synthesis of optically pure (S)-CHBE.  相似文献   

17.
The asymmetric reduction of ethyl 4-chloro-3-oxobutanoate (COBE) to ethyl (R)-4-chloro-3-hydroxybutanoate (CHBE) using Escherichia coli JM109 (pKAR) cells expressing the aldehyde reductase gene from Sporobolomyces salmonicolor AKU4429 as a catalyst was studied. The reduction required NADP+, glucose and glucose dehydrogenase for NADPH regeneration. In an aqueous system, the substrate was unstable, and inhibition of the reaction by the substrate was also observed. Efficient conversion of COBE to (R)-CHBE with a satisfactory enantiomeric excess (ee) was attained on incubation with transformant cells in an n-butyl acetate/water two-phase system containing the above NADPH-regeneration system. Under the optimized conditions, with the periodical addition of COBE, glucose and glucose dehydrogenase, the (R)-CHBE yield reached 1530 mM (255 mg/ml) in the organic phase, with a molar conversion yield of 91.1% and an optical purity of 91% ee. The calculated turnover of NADP+, based on the amounts of NADP+ added and CHBE formed, was about 5100 mol/mol. Received: 26 May 1997 / Received revision: 16 July 1997 / Accepted: 29 August 1997  相似文献   

18.
The enzymatic production of ethyl butyrate was studied: the lipase of Candida rugosa (E.C. 3.1.1.3.) was immobilized in a polyurethane matrix and subsequently introduced in an organic medium containing the substrates in appropriate concentrations. The large majority of experiments was carried out in n-hexane. Two further solvents were tested, namely n-heptane and n-dodecane. The partition coefficients matrix/solvent were estimated for the various solvent systems. The initial esterification rate, the molar yield ester/acid and the degree of conversion were found to be solvent independent when the reaction media were designed so that similar concentrations were created in the microenvironment. Initial rate experiments indicated that in n-hexane the threshold of inhibitory substrate concentrations lies (i) between 0.40 M and 0.50 M for butyric acid, according to the purity of the enzyme preparation and (ii) at 0.30 M for ethanol. Batch operational stability tests indicate that no enzyme deactivation occurs after 20 consecutive batches.  相似文献   

19.
An NADPH-dependent carbonyl reductase (S1) isolated from Candida magnoliae catalyzed the reduction of ethyl 4-chloro-3-oxobutanoate (COBE) to ethyl (S)-4-chloro-3-hydroxybutanoate (CHBE), with a 100% enantiomeric excess, which is a useful chiral building block for the synthesis of pharmaceuticals. The gene encoding the enzyme was cloned and sequenced. The S1 gene comprises 849 bp and encodes a polypeptide of 30,420 Da. The deduced amino acid sequence showed a high degree of similarity to those of the other members of the short-chain alcohol dehydrogenase superfamily. The S1 gene was overexpressed in Escherichia coli under the control of the lac promoter. The enzyme expressed in E. coli was purified to homogeneity and had the same catalytic properties as the enzyme from C. magnoliae did. An E. coli transformant reduced COBE to 125 g/l of (S)-CHBE, with an optical purity of 100% enantiomeric excess, in an organic solvent two-phase system.  相似文献   

20.
Fe3O4-Arg was selected as the optimal carrier due to its high activity recovery of immobilized cells in the preparation of Fe3O4-Arg-Cells. The optimal immobilization conditions for the preparation of Fe3O4-Arg-Cells were 30 °C, 4 h, pH 7, and 3 g dry yeast. The activity recovery of immobilized cells reached 76.8 %. For a batch reduction in a shaker in an alternating magnetic field, Fe3O4-Arg-Cells were used as a catalyst to gain ethyl (R)-4-chloro-3-hydroxybutyrate ((R)-CHBE). For further improvement in reduction productivity, a continuous reduction in the magnetic fluidized bed reactor system (MFBRS) was completed. Under their optimal transformation conditions, it took 24 h for Fe3O4-Arg-Cells to complete the conversion of ethyl 4-chloro-3-oxobutanoate (COBE) (0.8553 mol/L) in the shaker and only 8 h for the batch reduction in an alternating magnetic field. Continuous reduction in MFBRS provided new ideas for the efficient production of (R)-CHBE; 1.5882 mol/L (10 mL) of COBE can be completely converted in 6 h. The conversion and enantiomeric excess (e.e.) of (R)-CHBE were 100 % and above 99.9 % respectively, in the three reaction systems mentioned above.  相似文献   

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