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1.
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%。  相似文献   

2.
产环氧化物水解酶的黑曲霉菌种分离和发酵条件的研究   总被引:5,自引:0,他引:5  
沙倩  孙万儒等 《菌物系统》2001,20(4):494-502
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%。  相似文献   

3.
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.  相似文献   

4.
建立了一种快速筛选选择性水解手性芳香酰胺类化合物微生物的方法。在中性或弱碱性条件下,KMnO4能氧化芳香胺,但对芳香乙酰胺没有氧化效果。KMnO4被芳香胺还原而褪色,通过褪色程度来快速测定菌的酶活力及手性选择性。以1-苯基乙酰胺为例,得出最佳筛选体系:最大吸收波长为525 nm;1-苯基乙胺在0.04~5 mmol/L的浓度范围内与其ΔA525符合朗伯比尔定律;反应温度为60℃,反应时间为20 m in。通过该模型筛到5株选择性的菌株,R-选择性的菌株4株,S-选择性的菌株1株。  相似文献   

5.
应用混合菌系实现右旋磷霉素手性生物转化的初步研究   总被引:1,自引:0,他引:1  
探索了一条通过混合菌系把右旋磷霉素转化为左旋磷霉素的生物转化新途径。采用"右旋磷霉素利用菌"和"左旋磷霉素抗性菌"两种筛选模型,从某制药厂土壤中筛选到了7株右旋磷霉素利用菌和6株左旋磷霉素抗性菌。将上述13株菌混合接种到以0.5%右旋磷霉素为唯一碳源的无机盐培养基中,30℃、150r/min培养3~5d,经磷霉素敏感菌生物检测、薄层层析(TLC)检测,初步确证了转化产物中存在左旋磷霉素。对右旋磷霉素的手性生物转化条件进行了初步探索,发现接种时带入少量肉汤培养基对转化有促进作用,而微量元素Co~(2-)和VO_3~-对转化没有促进作用。为在磷霉素生产中减少资源浪费和提高产量提供了理论依据。  相似文献   

6.
【目的】通过定点突变技术,改变近平滑假丝酵母短链羰基还原酶Ⅱ(SCRⅡ)催化苯乙酮衍生物的功能,为数种手性芳香醇的生产提供一种高效、安全的新型制备方法。【方法】通过氨基酸序列和蛋白结构比对的方法,选择SCRⅡ的底物结合域中关键氨基酸位点E228实施突变,构建相应的突变株Escherichia coliBL21/pET28a-E228S;以苯乙酮衍生物为底物,对突变株的酶活和生物转化功能进行了分析。【结果】酶活测定结果表明:突变株E.coli BL21/pET28a-E228S催化原始底物2-羟基苯乙酮的酶活仅为原始酶活的25%左右;而催化苯乙酮、4’-甲基苯乙酮、4’-氯苯乙酮的酶活是突变前的7-20倍。突变株E.coli BL21/pET28a-E228S生物转化2-羟基苯乙酮,获得产物(S)-苯基乙二醇的得率不超过10%,而以苯乙酮、4’-甲基苯乙酮、4’-氯苯乙酮为底物时,生物转化产物光学纯度维持在99%,得率高达80%以上。【结论】对底物结合域中的关键氨基酸实施突变,提高了SCRⅡ催化苯乙酮衍生物的底物广谱性,拓展了该酶的生物功能,为理性改造短链羰基还原酶的不对称还原催化功能和手性芳香醇的制备提供了新型途径。  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.
D型氨基酸氧化酶活性对于D-硝基精氨酸手性转化的影响   总被引:1,自引:0,他引:1  
D-硝基精氨酸(D-NNA)可在大鼠体内发生手性转化生成其L型异构体,即L-NNA,后者可抑制一氧化氮合酶活性,减少一氧化氮生成,升高动脉血压.研究了D型氨基酸氧化酶(DAAO)在D-NNA手性转化中的作用及DAAO对不同(包括已报道在体内可发生手型转化的)D型氨基酸的选择活性.体内实验显示,DAAO的选择性抑制剂苯甲酸钠(400mg/kg)或肌酐(400mg/kg)均可在不同程度上抑制D-NNA升压作用,进一步研究发现,肾脏或肝脏DAAO酶液在外加DAAO后可提高D-NNA的手性转化约2倍,表明DAAO对于D-NNA在体内的手性转化是必需的.DAAO酶液对可在体内发生手性转化且转化率相似(30%~50%)的D型氨基酸(D-Phe,D-Leu和D-NNA)的选择性表现出显著差异(Kcat/Km相差可达约15倍左右),这从另一方面表明体内D-硝基精氨酸氧化是其发生手性转化的前提条件但非决定因素.  相似文献   

9.
含芳香基手性醇是许多手性药物合成的关键手性砌块,生物催化不对称还原前手性酮是合成该类醇的重要方法之一.以4'-氯-苯乙酮为模型底物,从土壤中筛选得到一株能高效催化前手性芳香酮不对称还原合成相应手性醇的菌株,鉴定表明该菌株为白地霉( Geotrichum candid ).进一步考察了其催化4'-氯-苯乙酮不对称还原的反应特性,发现还原4'-氯-苯乙酮的产物主要为 S-4'-氯苯乙醇.在合适的反应条件下,其产率达到35%,对映选择性高于97%.  相似文献   

10.
经5轮诱变筛选,从近平滑假丝酵母(Candida parapsilosis CICC1676)中分离得到产NADH依赖型羰基还原酶(Carbonyl reductase,CR)菌株CP-9。所产羰基还原酶(CRCp-9)经两步快速纯化获得纯化倍数为11.5倍,比活力为1.84 U/mg的酶液,其还原反应的最适pH值为6.5,最适温度为40℃。该酶转化β-羟基苯乙酮制备手性化合物(R)-苯基乙二醇,因此是(R)-专一性羰基还原酶。该酶与NADH普适性再生酶-甲酸脱氢酶(For-mate dehydrogenase,FDH)在胞外相耦联,构建伴有辅酶再生与反复利用的CR/FDH双酶催化制备立体醇体系,底物β-羟基苯乙酮转化率达95.4%,产物(R)-苯基乙二醇得率为93%,辅酶的总转化数(Total turn number, TTN)达267,产物e.e.值为98.6%,批次耦合反应生产能力达0.8 g/L/h,较单酶催化有较大提高,与细胞转化法相比也具有较好的生产能力。因此,伴有辅酶再生的胞外酶耦合催化具有潜在的制备手性醇化合物的工业应用价值。  相似文献   

11.
Yeast strains (410) from more than 45 different genera were screened for the enantioselective hydrolysis of nitro substituted styrene oxides. These strains included 262 yeasts with known epoxides hydrolase activity for various other epoxides. Epoxide hydrolase activity for p-nitrostyrene oxide (pNSO) (177 strains) and m-nitrostyrene oxide (mNSO) (148 strains) was widespread in the yeasts, while activity for o-nitrostyrene oxide (oNSO) was less ubiquitous (22 strains). The strains that displayed enantioselectivity in the hydrolysis of one or more of the nitro substituted styrene oxides (35 strains) were also screened against styrene oxide (SO). Rhodosporidium toruloides UOFS Y-0471 displayed the highest enantioselectivity for pNSO (ee 55%, yield 35%) while Rhodotorula glutinis UOFS Y-0653 displayed the highest enantioselectivity for mNSO (ee >98%, yield 29%), oNSO (ee 39%, yield 19%) and SO (ee >98%, yield 19%). (R)-Styrene oxide was preferentially hydrolysed to the corresponding (R)-diol with retention of configuration at the stereogenic centre. In the case of the nitro substituted styrene oxides the absolute configurations of the remaining epoxides and the formed diols were not established.  相似文献   

12.
ABSTRACT

The AcrAB-TolC efflux pump is involved in the organic solvent tolerance of Escherichia coli. Most E. coli strains are highly sensitive to organic solvents such as n-hexane and cyclohexane. Here, a recombinant E. coli transformed with an expression plasmid containing acrAB and tolC became tolerant to n-hexane and cyclohexane. The levels of AcrA, AcrB, and TolC in the recombinant increased by 3- to 5-fold compared to those in the control strain without the plasmid for acrAB or tolC. To investigate the usability of the recombinant as a biocatalyst in an aqueous-organic solvent two-phase system, we further introduced xylMA xylene monooxygenase genes from Pseudomonas putida mt-2 into the recombinant and examined the production of styrene oxide from styrene. The resulting recombinant produced 1.8 mg and 1.0 mg styrene oxide mL?1 of medium in a medium overlaid with a 25% volume of n-hexane and cyclohexane containing 10% (wt vol?1) styrene, respectively.  相似文献   

13.
The formation of optically pure styrene oxides by oxidation of styrene and the isomerisation of styrene oxide to phenylacetaldehyde was investigated with different microorganisms.  相似文献   

14.
Styrene oxide isomerase (SOI) [EC 5.3.99.7], most probably located in the cell wall, was partially purified from Coiynebacterium sp. AC-5 cells grown in a styrene gas atmospheres. The enzyme catalyzed the isomerization reaction to give phenylacetaldehyde, but did not catalyze its reverse reaction. The optimum pH of the reaction was around 7.0, and the enzyme was unstable below pH 6.0. The Km toward styrene oxide was very low (7.7 × 10?5 m), indicating its high affinity for styrene oxide. The enzyme showed strict substrate specificity, and epoxide compounds other than styrene oxide did not serve as substrates. (S)-Styrene oxide was preferentially converted by the enzyme, compared with the (R)-isomer. The possible application of SOI as a biocatalyst is also discussed.  相似文献   

15.
By using styrene as the sole source of carbon and energy in concentrations of 10 to 500 microM, 14 strains of aerobic bacteria and two strains of fungi were isolated from various soil and water samples. In cell extracts of 11 of the bacterial isolates, a novel flavin adenine dinucleotide-requiring styrene monooxygenase activity that oxidized styrene to styrene oxide (phenyl oxirane) was detected. In one bacterial strain (S5), styrene metabolism was studied in more detail. In addition to styrene monooxygenase, cell extracts from strain S5 contained styrene oxide isomerase and phenylacetaldehyde dehydrogenase activities. A pathway for styrene degradation via styrene oxide and phenylacetaldehyde to phenylacetic acid is proposed.  相似文献   

16.
By using styrene as the sole source of carbon and energy in concentrations of 10 to 500 microM, 14 strains of aerobic bacteria and two strains of fungi were isolated from various soil and water samples. In cell extracts of 11 of the bacterial isolates, a novel flavin adenine dinucleotide-requiring styrene monooxygenase activity that oxidized styrene to styrene oxide (phenyl oxirane) was detected. In one bacterial strain (S5), styrene metabolism was studied in more detail. In addition to styrene monooxygenase, cell extracts from strain S5 contained styrene oxide isomerase and phenylacetaldehyde dehydrogenase activities. A pathway for styrene degradation via styrene oxide and phenylacetaldehyde to phenylacetic acid is proposed.  相似文献   

17.
Recombinant Escherichia coli JM101(pSPZ10) cells produce the styrene monooxygenase of Pseudomonas sp. strain VLB120, which catalyzes the oxidation of styrene to (S)-styrene oxide at an enantiomeric excess larger than 99%. This biocatalyst was used to produce 388 g of styrene oxide in a two-liquid phase 30-L fed-batch bioconversion. The average overall volumetric activity was 170 U per liter over a period of more than 10 h, equivalent to mass transfer rates of 10.2 mmoles per liter per hour at a phase ratio of 0.5. At this transfer rate, the biotransformation system appeared to be substrate mass-transfer limited. The reactor had an estimated power input in the order of 5 W. L(-1), which is close to values typically obtained with commercially operating units. The product could be easily purified by fractional distillation to a purity in excess of 97%. The process illustrates the feasibility of recombinant whole cell biotransformations in two-liquid phase systems with toxic substrates and products.  相似文献   

18.
Soluble epoxide hydrolase (EH) from the potato Solanum tuberosum and an evolved EH of the bacterium Agrobacterium radiobacter AD1, EchA-I219F, were purified for the enantioconvergent hydrolysis of racemic styrene oxide into the single product (R)-1-phenyl-1,2-ethanediol, which is an important intermediate for pharmaceuticals. EchA-I219F has enhanced enantioselectivity (enantiomeric ratio of 91 based on products) for converting (R)-styrene oxide to (R)-1-phenyl-1,2-ethanediol (2.0 +/- 0.2 micromol/min/mg), and the potato EH converts (S)-styrene oxide primarily to the same enantiomer, (R)-1-phenyl-1,2-ethanediol (22 +/- 1 micromol/min/mg), with an enantiomeric ratio of 40 +/- 17 (based on substrates). By mixing these two purified enzymes, inexpensive racemic styrene oxide (5 mM) was converted at 100% yield to 98% enantiomeric excess (R)-1-phenyl-1,2-ethanediol at 4.7 +/- 0.7 micromol/min/mg. Hence, at least 99% of substrate is converted into a single stereospecific product at a rapid rate.  相似文献   

19.
Styrene oxide-cysteine adduction is predominantly involved in protein covalent modification after exposure in vivo to styrene or styrene oxide. In the present study, we developed an alkaline permethylation- and GC/MS-based approach to detect styrene oxide-derived protein adduction. Permethylation of the protein adducts produced two methylthiophenylethanols, namely 2-methylthio-2-phenyl-1-ethanol and 2-methylthio-1-phenyl-1-ethanol. To improve the permethylation efficiency, reaction conditions, including temperature, time, NaOH strength, and molar ratio of CH3I/NaOH, were explored. Under optimized conditions, the yields of the analyte formation resulting from permethylation of authentic standard α- and β-mercapturic acids, representing α and β isomers of cysteine adducts, were 35% and 28%, respectively. Permethylation of styrene oxide-modified bovine serum albumin released the two methylthiophenylethanols with an α-/β-adduction ratio of 1.5. A concentration-dependent increase in both α- and β-adduction was observed in mouse liver microsomes incubated with styrene at various concentrations. CD-1 mice were administered intraperitoneally with styrene at doses of 0, 50, and 400 mg/kg daily for 5 days. The formation of protein adducts derived from styrene oxide in whole blood in 400 mg/kg group was observed with an α/β ratio of 4.8, suggesting that the reaction of styrene oxide with cysteine residues took place more likely at the α-carbon than the β-carbon of styrene oxide.  相似文献   

20.
We performed a macrokinetic and quantitative microbial investigation of a continuously operating bench-scale biofilter treating styrene-polluted gases. The device was filled with a mixture of peat and glass beads as packing medium and inoculated with the styrene-oxidizing strain, Rhodococcus rhodochrous AL NCIMB 13259. The experimental data of styrene and microbial concentrations, obtained at different biofilter heights, were used to evaluate the pollutant concentration profiles as well as the influence of styrene loading on biomass distribution along the packing medium. Styrene and biomass concentration profiles permitted detection of a linear relationship between the amount of biomass grown in a given section of the biofilter and that of pollutant removed, regardless of the operating conditions tested. Biomass development in the bed appeared to: depend linearly on pollutant concentration at an inlet styrene concentration of <0.10 g m(-3) in the gaseous stream; achieve a maximum value (7. 10(7) colony forming units per gram of packing material) within a wide styrene concentration range (0.10 to 1.0 g m(-3)); and fall sharply beyond this inhibition threshold. The process followed zeroth-order macrokinetics with respect to styrene concentration, which is consistent with zeroth-order microkinetics with either fully active or not fully active biofilm. The maximal volumetric styrene removal rate was found to be 63 g m(packing material) (-3) h(-1) for an influent pollutant concentration of 0.80 g m(-3) and a superficial gas velocity of 245 m h(-1).  相似文献   

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