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%。     

应用合成生物学策略构建全细胞生物催化剂合成(S)-乙偶姻

目的:在大肠杆菌宿主中过量表达丁二酮还原酶(DAR),同时构建辅酶NADH原位再生系统,利用全细胞高效催化丁二酮不对称还原合成(S)-乙偶姻。方法:PCR克隆多黏芽孢杆菌(Paenibacillus polymyxa) dar基因连到质粒pETDuet-1,转化至大肠杆菌(Escherichia coli) BL21(DE3),构建重组菌E. coli BL21(DE3)-DAR;通过Hi Trap TALON柱亲和层析纯化表达产物DAR酶蛋白,测定DAR的比酶活和分子动力学参数。在重组菌E. coli BL21(DE3)-DAR中构建辅酶NADH原位再生系统,协同表达枯草芽孢杆菌(Bacillus subtilis)的葡萄糖脱氢酶(GDH),构建重组菌E. coli BL21(DE3)-DAR/GDH,并以此重组菌为全细胞生物催化剂,优化催化条件,提高(S)-乙偶姻的产量和产率。结果:获得重组工程菌E. coli BL21(DE3)-DAR和E. coli BL21(DE3)-DAR/GDH。DAR以NADH为辅酶还原丁二酮的米氏常数Km、最大催化速率Vmax、催化常数Kcat分别为2. 59mmol/L、1. 64μmol/(L·min·mg)、12. 3/s,还原丁二酮生成(S)-乙偶姻光学的纯度为95. 86%,具有较好的催化效率和立体异构体选择性。构建辅酶NADH原位再生系统后,重组菌E. coli BL21(DE3)-DAR/GDH可高效催化丁二酮合成乙偶姻。在最优催化条件下分批补料,乙偶姻产量达51. 26g/L,转化率为81. 37%,生产速率为5. 13g/(L·h)。结论:使用非手性化合物原料丁二酮生产高附加值的手性化合物(S)-乙偶姻,以重组菌为全细胞生物催化剂合成(S)-乙偶姻,不需额外添加昂贵的辅酶,具有较高的生产应用价值。     

基于己糖激酶与葡萄糖-6-磷酸脱氢酶共表达的辅酶NADPH高效再生

【目的】构建己糖激酶与葡萄糖-6-磷酸脱氢酶的大肠杆菌共表达体系,以葡萄糖为底物实现辅酶NADPH的高效再生。【方法】通过分子生物学方法,克隆己糖激酶HKgs、HKpp基因,并于Escherichia coli BL21(DE3)中表达,再将己糖激酶HKgs、HKpp分别与葡萄糖-6-磷酸脱氢酶Gpd PP共表达,实现NADPH的原位再生。比较两个共表达工程菌的辅酶再生效果,并针对催化活力较高的工程菌BL21(HKgs+Gpd PP)进行表达条件优化。【结果】NADPH再生活力达到856 U/L。该辅酶再生体系与醇脱氢酶Adh R联合催化,使不对称还原4-氯乙酰乙酸乙酯的催化活力提高至原始值的2.5倍。【结论】通过己糖激酶与葡萄糖-6-磷酸脱氢酶在大肠杆菌中的共表达,构建了一个新的NADPH高效再生体系,并用于醇脱氢酶催化的不对称还原反应。     

丙酮酸脱羧酶基因和乙醇脱氢酶基因表达载体的构建

以运动发酵单胞菌(Zymomonas mobilis)的总DNA为模板,PCR扩增运动发酵单胞菌中的丙酮酸脱羧酶( Pyruvate decarboxylase,PDC)基因和乙醇脱氢酶Ⅱ(Alcohol dehydrogenaseⅡ,ADHⅡ)基因.将丙酮酸脱羧酶基因和含核糖体结合位点(RBS)的乙醇脱氢酶基因串联起来置于T7启动子控制下,构成多顺反子表达质粒pQR-PRA.经酶切和PCR验证,表达载体构建成功.将pQR-PRA转入大肠埃希菌(Escherichia coli)BL21中,转化子的定性检测表明有酶表达,并且初步测定了2种酶的表达量.     

(R)-专一性羰基还原酶与甲酸脱氢酶基因在大肠杆菌中的共表达

【目的】通过研究(R)-专一性羰基还原酶和甲酸脱氢酶基因在大肠杆菌中的共表达，解决较高底物浓度下不对称转化反应的辅酶限制性问题。【方法】分别以近平滑假丝酵母(Candida parapsilosis CCTCC M203011)和博伊丁假丝酵母(Candida boidinii)基因组为模板，采用PCR方法扩增得到(R)-专一性羰基还原酶基因（rcr）和甲酸脱氢酶基因（fdh），克隆到共表达载体pETDuetTM-1中进行表达。共表达质粒pETDuet-rcr-fdh转化稀有密码子优化型菌株E. coli Rosetta，获得重组菌E. coli Rosetta/pETDuet-rcr-fdh。【结果】在30℃条件下，经1 mmol/L IPTG诱导表达8 h后，SDS-PAGE结果表明(R)-专一性羰基还原酶和甲酸脱氢酶均有明显的表达，其相对分子质量分别为37 kDa和 40 kDa。以高浓度(6 g/L)2-羟基苯乙酮为底物时，0.1 g重组菌细胞催化产生(R)-苯基乙二醇，产物光学纯度为100% e.e.，产率为85.9%。与无甲酸脱氢酶参与辅酶再生循环的重组菌E. coli Rosetta/pETDuet-rcr相比，产物光学纯度和产率分别提高了1.3和2.7倍。【讨论】该重组菌的构建为基因工程法生物合成(R)-苯基乙二醇的工业应用奠定了基础。     

构建伴有β-葡萄糖苷酶表达的乙醇发酵大肠杆菌

研究构建能够分泌表达纤维素酶的产乙醇菌株,实现降解木质纤维素生产乙醇的整合生物加工过程。文中通过克隆来自运动发酵单胞菌Zymomonas mobilis ZM4的丙酮酸脱羧酶基因pdc和乙醇脱氢酶基因adhB,并通过Red重组将二者整合到大肠杆菌Escherichia coli JM109基因组中,首先构建了一株可以利用葡萄糖进行乙醇发酵的重组菌E. coli P81。随后将来源于多粘芽胞杆菌Bacillus polymyxa1.794的β-葡萄糖苷酶基因bglB在E. coli P81中进行了分泌表达,得到了一株可以进行纤维二糖降解和乙醇发酵双重功能的重组菌E. coli P81(pUC19-bglB)。该菌胞外分泌β-糖苷酶活达到84.78 mU/mL菌液,纤维二糖酶活达到了32.32 mU/mL菌液。该重组菌E. coli P81(pUC19-bglB) 以纤维二糖为碳源进行乙醇发酵,乙醇得率达到了理论产率55.8％,而在葡萄糖和纤维二糖的共发酵中,其乙醇产量达到了理论产率46.5％。构建得到的此株整合生物加工大肠杆菌能够利用β-葡萄糖苷酶生产乙醇,为构建能利用木质纤维素分解产物生产燃料乙醇的高效、稳定生产用工程菌奠定了良好的基础。     

亮氨酸脱氢酶C端Loop区域的理性设计及多酶级联高效合成l-2-氨基丁酸

亮氨酸脱氢酶 (Leucine dehydrogenase,LDH) 是制备l-2-氨基丁酸的关键限速酶,针对该酶的Loop区域进行改造以提高关键酶的酶活及稳定性从而高效合成l-2-氨基丁酸。通过亮氨酸脱氢酶的分子动力学模拟分析均方根涨落 (Root mean square fluctuation,RMSF) 值,对其波动非常明显的Loop区域合理设计以得到比酶活提高的截短突变体EsLDHD2,其比酶活为野生型的123.2%;此外,由于l-2-氨基丁酸制备过程中苏氨酸脱氨酶催化l-苏氨酸制备2-酮丁酸的速率过快导致多酶催化不平衡,因此双拷贝亮氨酸脱氢酶及甲酸脱氢酶以平衡多酶催化速率,构建多酶级联催化的单细胞E. coli BL21/pACYCDuet-RM,其摩尔转化率相较于E. coli BL21/pACYCDuet-RO提高74.6%;对菌株E. coli BL21/pACYCDuet-RM的全细胞转化条件进行优化,其最适pH、温度、底物浓度分别为7.5、35 ℃和80 g/L,此时摩尔转化率大于99%;在1 L转化体系和最适转化条件下分批加入l-苏氨酸80 g和40 g,l-2-氨基丁酸的产量达97.2 g。总之,该策略为l-2-氨基丁酸的制备提供了绿色、高效的合成方法,具有工业化制备药物前体的巨大潜力。     

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.     

3-甾酮-1-脱氢酶在不同表达体系中的表达研究

简单节杆菌3-甾酮-1-脱氢酶(KSDH),是甾体母核降解的关键酶,属于黄素蛋白类,并且是一种膜蛋白。膜蛋白的高效表达一直是一个难题。本文尝试利用三种不同的大肠杆菌表达体系,pET-30a/BL21(DE3)、pET-40b( )/BL21(DE3)和pTrc99A/JM109对C1,2位脱氢酶进行诱导表达,并对蛋白的表达量和酶活力进行比较分析,确定出最适的表达系统。     

Industrial production of (R)-1,3-butanediol by new biocatalysts

We have developed the economical and convenient biocatalytic process for the preparation of (R)-1,3-butanediol (BDO) by stereo-specific microbial oxido-reduction on an industrial scale. (R)-1,3-BDO is an important chiral synthon for the synthesis of various optically active compounds such as azetidinone derivatives lead to penem and carbapenem antibiotics.

We studied on two approaches to obtain (R)-1,3-BDO. The first approach was based on enzyme-catalyzed asymmetric reduction of 4-hydroxy-2-butanone; the second approach was based on enantio-selective oxidation of the undesired (S)-1,3-BDO in the racemate. As a result of screening for yeasts, fungi and bacteria, the enzymatic resolution of racemic 1,3-BDO by the Candida parapsilosis IFO 1396, which showed differential rates of oxidation for two enantiomers, was found to be the most practical process to produce (R)-1,3-BDO with high enantiomeric excess and yield.

We characterized the (S)-1,3-BDO dehydrogenase purified from a cell-free extract of C. parapsilosis. This enzyme was found to be a novel secondary alcohol dehydrogenase (CpSADH). We have attempted to clone and characterize the gene encoding CpSADH and express it in Escherichia coli. The CpSADH activity of a recombinant E. coli strain was more than two times higher than that of C. parapsilosis. The production yield of (R)-1,3-BDO from the racemate increased by using the recombinant E. coli strain. Interestingly, we found that the recombinant E. coli strain catalyzed the reduction of ethyl 4-chloro-3-oxo-butanoate to ethyl (R)-4-chloro-3-hyroxy-butanoate with high enantiomeric excess.     

Crystal structure of (R)-3-hydroxybutyryl-CoA dehydrogenase PhaB from Ralstonia eutropha

(R)-3-hydroxybutyryl-CoA dehydrogenase PhaB from Ralstonia eutropha H16 (RePhaB) is an enzyme that catalyzes the NADPH-dependent reduction of acetoacetyl-CoA, an intermediate of polyhydroxyalkanoates (PHA) synthetic pathways. Polymeric PHA is used to make bioplastics, implant biomaterials, and biofuels. Here, we report the crystal structures of RePhaB apoenzyme and in complex with either NADP⁺ or acetoacetyl-CoA, which provide the catalytic mechanism of the protein. RePhaB contains a Rossmann fold and a Clamp domain for binding of NADP⁺ and acetoacetyl-CoA, respectively. The NADP⁺-bound form of RePhaB structure reveals that the protein has a unique cofactor binding mode. Interestingly, in the RePhaB structure in complex with acetoacetyl-CoA, the conformation of the Clamp domain, especially the Clamp-lid, undergoes a large structural change about 4.6 Å leading to formation of the substrate pocket. These structural observations, along with the biochemical experiments, suggest that movement of the Clamp-lid enables the substrate binding and ensures the acetoacetyl moiety is located near to the nicotinamide ring of NADP⁺.     

Kinetic properties of N-(2-carboxyethyl)-NAD(H) and poly(ethylene glycol)-bound NAD(H) for alcohol, lactate, malate and glyceraldehyde-3-phosphate dehydrogenase from different organisms

The steady-state kinetics of alcohol dehydrogenases (alcohol:NAD⁺ oxidoreductase, EC 1.1.1.1 and alcohol:NADP⁺ oxidoreductase, EC 1.1.1.2), lactate dehydrogenases (l-lactate:NAD⁺ oxidoreductase, EC 1.1.1.27 and d-lactate:NAD⁺ oxidoreductase, EC 1.1.1.28), malate dehydrogenase (l-malate:NAD⁺ oxidoreductase, EC 1.1.1.37), and glyceraldehyde-3-phosphate dehydrogenases [d-glyceraldehyde-3-phosphate:NAD⁺ oxidoreductase (phosphorylating), EC 1.2.1.12] from different sources (prokaryote and eukaryote, mesophilic and thermophilic organisms) have been studied using NAD(H), N⁶-(2-carboxyethyl)-NAD(H), and poly(ethylene glycol)-bound NAD(H) as coenzymes. The kinetic constants for NAD(H) were changed by carboxyethylation of the 6-amino group of the adenine ring and by conversion to macromolecular form. Enzymes from thermophilic bacteria showed especially high activities for the derivatives. The relative values of the maximum velocity (NAD = 1) of Thermus thermophilus malate dehydrogenase for N⁶-(2-carboxyethyl)-NAD and poly(ethylene glycol)-bound NAD were 5.7 and 1.9, respectively, and that of Bacillus stearothermophilus glyceraldehyde-3-phosphate dehydrogenase for poly(ethylene glycol)-bound NAD was 1.9.     

Biotransformation of a crizotinib intermediate using a mutant alcohol dehydrogenase of Lactobacillus kefir coupled with glucose dehydrogenase

Abstract

(S)-1-(2, 6-dichloro-3-fluorophenyl) ethanol, the key chiral intermediate of crizotinib, was prepared from 1-(2, 6-dichloro-3-fluorophenyl) ethanone using the alcohol dehydrogenases from Lactobacillus kefir (ADH-LK) with a tetrad mutant (ADH-LKM, F147L/Y190P/V196L/A202W), coupled with glucose dehydrogenase (GDH). In the present study, ADH-LKM and GDH were successfully heterologous expressed in recombinant Escherichia coli. During the regeneration of NADPH with GDH, 150?g/L substrate was totally transformed into target chiral alcohol with an enantiomeric excess value of 99.9% after 12?h at 30?°C (pH 7.0). Our study demonstrates the potential for industrial green production of the key chiral intermediate of crizotinib.     

Regiospecific hydroxylation of 3-(methylaminomethyl) pyridine to 5-(methylaminomethyl) -2 (1H) -pyridinone byArthrobacter ureafaciens

Microbial production of a 6-hydroxy-3-pyridylmethyl compound from 3-pyridylmethyl compound was investigated. The hydroxylation of 3-(methylaminomethyl)pyridine to 5-(methylaminomethyl)-2(1H)-pyridinone, tautomer of 2-hydroxy-5(methylaminomethyl)pyridine, by resting cells ofArthrobacter ureafaciens JCM3873 was found to proceed regio- and chemo-selectively with an almost quantitative yield. The addition of molybdate ion and nicotine as an inducer to the culture medium was required for the preparation of cells containing high hydroxylation activity. The optimal temperature and pH for the hydroxylation by using resting cells were 35°C and around 7, respectively. This hydroxylation enzyme does undergo inhibition by the substrate. The inhibitory effect could be eliminated by stepwise feeding of the substrate. Under adequate conditions, 23 mg/ml of 5-(methylaminomethyl)-2(1H)-pyridinone was produced with a molar yield of nearly 100% from 3-(methylaminomethyl)pyridine.     

Production of poly-D(-)-3-hydroxybutyrate and poly-D(-)-3-hydroxyvalerate by strains ofAlcaligenes latus

Alcaligenes latus strains can accumulate poly-D(-)-3-hydroxybutyrate (PHB) up to about 85% of cell dry weight. The abilities to store poly-D(-)-3-hydroxyvalerate (PHV) of three strains ofA. latus were investigated. With Na-propionate as PHV precursor, strainA. latusDSM 1122 had better PHV accumulation ability than strainsA. latusDSM 1123 and 1124. StrainA. latus DSM 1123 could store PHV when Na-valerate but not Na-propionate served as the PHV precursor. PHB and PHV accumulation byA. latus DSM 1124 rapidly increased when propionic acid and acetic acid were together added to the fermentor. This increase was not obtained in the culture shaker flask and fermentor growing the same strain when Na-propionate alone served as a PHV precursor.     

酿酒酵母by1.1b产D-(-)-扁桃酸脱氢酶的发酵条件优化

对一株产D-(-)-扁桃酸对映选择性脱氢酶的酿酒酵母菌(Saccharomyces cerevisiae sp. strain by1.1b)发酵产酶条件进行了优化。研究各种碳源、氮源及无机盐对产酶的影响, 应用正交试验优化发酵培养基组成, 结果为: 蛋白胨 60 g/L, 麦芽糖 30 g/L, MgSO4 0.5 g/L, ZnSO4 0.01 g/L, KCl 1.0 g/L。优化后酶产量提高了7.9倍(由2.56 U/mL增至20.21 U/mL)。摇瓶培养最佳条件为: 装液量40 %, 发酵pH 6.5, 接种量10 %, 发酵温度30 ℃。考察了细胞生长及产酶的时间进程, 最佳培养时间为25 h。     

酿酒酵母by1.1b产D-(-)-扁桃酸脱氢酶的发酵条件优化

对一株产D-(-)-扁桃酸对映选择性脱氢酶的酿酒酵母菌(Saccharomyces cerevisiae sp.strain by1.1b)发酵产酶条件进行了优化.研究各种碳源、氮源及无机盐对产酶的影响,应用正交试验优化发酵培养基组成,结果为:蛋白胨60 g/L,麦芽糖30 g/L,MgSO4 0.5 g/L,ZnSO4 0.01 g/L,KCl 1.0 g/L.优化后酶产量提高了7.9倍(由2.56 U/mL增至20.21 U/mL).摇瓶培养最佳条件为:装液量40%,发酵pH 6.5,接种量10%,发酵温度30℃.考察了细胞生长及产酶的时间进程,最佳培养时间为25 h.     

(E)-2-(2-(2-hydroxyphenyl)hydrazono)-1-phenylbutane-1,3-dione: Tautomery and coordination to copper(II)

(E)-2-(2-(2-hydroxyphenyl)hydrazono)-1-phenylbutane-1,3-dione (H₂L) was synthesized by azocoupling of diazonium salt of 2-hydroxyaniline with 1-phenylbutane-1,3-dione and characterized by IR, ¹H and ¹³C NMR spectroscopies and X-ray diffraction analysis. In solution, H₂L exists as a mixture of the enol-azo and hydrazone tautomeric forms and a decrease of temperature and of solvent polarity shifts the tautomeric balance to the hydrazone form. In the solid state, H₂L crystallizes from ethanol-water in the monohydrate hydrazone form, as shown by X-ray analysis. The dissociation constants of H₂L (pK₁ = 5.98 ± 0.04, pK₂ = 9.72 ± 0.03) and the stability constants of its copper(II) complex (log β₁ = 11.01 ± 0.07, log β₂ = 20.19 ± 0.08) were determined by the potentiometric method in aqueous-ethanol solution. The copper(II) complex [Cu₂(μ-L)₂]_n was isolated in the solid state and found by X-rays to be a coordination polymer of a binuclear core with a distorted square pyramidal metal coordination geometry.     

A Pitfall of the 3-(4,5-dimethylthiazol-2-yl)-5(3-carboxymethonyphenol)-2-(4-sulfophenyl)-2H-tetrazolium (MTS) Assay due to Evaporation in wells on the Edge of a 96 well Plate

The 3-(4,5-dimethylthiazol-2-yl)-5(3-carboxymethonyphenol)-2-(4-sulfophenyl)-2H-tetrazolium (MTS) calorimetric assay is replacing the traditional 3-(4,5-dimethylthiazol-2-yl)-2,5-diphenyltetrazolium bromide (MTT) assay as a fast, one-step assay of cell viability. We have observed that evaporation of the outer wells of a 96 well plate increases the absorbancy by 52% compared to the inner wells. Filling the outer 2 rows of wells with media and replacement of the media prior to addition of the MTS reagent will, however, correct this inaccuracy.