（S）-（-）-β-羟基苯丙酸乙酯的微生物法合成

采用酿酒酵母CGMCC No．2266菌体,不对称还原β-羰基苯丙酸乙酯制备光学纯（S）-（-）-β-羟基苯丙酸乙酯。结果表明：采用初始pH为8．0的液体发酵培养基培养的CGMCCNo．2266菌体经过50℃预热处理30min后用于生物转化获得的（S）-（-）-G-羟基苯丙酸乙酯对映体过剩值可以达到100％ee。确定了合成（S）-（-）-β-羟基苯丙酸乙酯的较佳转化条件为pH7．0,温度30℃,转化时间24h,底物浓度为3．63mmol／L,菌体用量为86g/L（干重／反应体积）。以10％葡萄糖为辅助底物,产率比不加辅助底物时提高了75．4％。在最佳转化条件下反应转化率及（S）-（-）-β-羟基苯丙酸乙酯对映体过剩值可分别达到98．4％和100％ee。     

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%。     

一菌双酶法制备L-4-氟苯丙氨酸

利用重组E．coli产天冬氨酸酶和天冬氨酸转氨酶催化生产L-4-氧苯丙氨酸的工艺。实验结果表明最佳转化条件为-37℃,pH值4．5—8．5,菌体与酮酸的质量浓度比为1.5,CTAB的质量分数为0．04％,酮酸的质量浓度11．28g／L,富马酸铵与酮酸的摩尔比为3．0：1．0,添加1mmol／L的Fe^2＋,L-天冬氨酸与酮酸的摩尔比为0．4：1。在最适条件下,经过14h酶转化反应达到平衡,酮酸转化率可达到95％以上,L-4-氟苯丙氨酸得率也可达到80％以上。此法原料简单易得,为L-4-氟苯丙氨酸的制备提供了一种新方法：     

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%。     

固定化细胞拆分(R,S)-α-乙基-2-氧-1-吡咯烷乙酸甲酯的研究

【目的】筛选鉴定一株产酯酶用于选择性拆分(R,S)-α-乙基-2-氧-1-吡咯烷乙酸甲酯的菌株,利用该菌株固定化细胞催化拆分外消旋底物。【方法】通过富集培养、罗丹明B平板初筛及复筛培养获得一株选择性拆分(R,S)-α-乙基-2-氧-1-吡咯烷乙酸甲酯的菌株,通过对其形态、生理生化特征及16S r DNA序列分析,确立该菌株系统发育地位。优化了利用硅藻土-戊二醛吸附交联法对该菌体细胞固定化的条件,研究固定化细胞催化性质及操作稳定性。【结果】该菌为革兰氏阴性菌,鉴定其为甲基球状菌属(Methylopila)。固定化体系最优条件:聚乙烯亚胺0.15%(V/V),戊二醛0.2%(V/V),硅藻土6 g/L,菌体质量浓度100 g/L。与游离细胞相比,固定化细胞最适p H由8.0变为8.5,最适温度由35°C变为40°C,p H稳定性和温度稳定性都有所提高。Cu~(2+)、Mn~(2+)、Ca~(2+)能促进酶活,Zn~(2+)、Fe~(2+)抑制酶活。固定化细胞的有机溶剂耐受性较游离细胞有所提高。动力学分析细胞固定化后Km值变大,底物亲和力降低。利用固定化细胞水解(R,S)-α-乙基-2-氧-1-吡咯烷乙酸甲酯,底物浓度200 g/L,反应20 h,保留构型为S型,得率47.8%,对映体过量值ees为99.4%,重复使用12次后仍保留初始酶活的80%以上。【结论】开发了利用Methylopila sp.cxzy-L013固定化细胞择性拆分(R,S)-α-乙基-2-氧-1-吡咯烷乙酸甲酯的工艺,该工艺具有良好的工业应用前景。     

利用固定化简单节杆菌转化醋酸可的松

用聚乙烯醇－海藻酸钙复合载体包埋简单节杆菌BY 2—3—5l的方法,制备了具有较高机械强度和较好活性的球形固定化细胞。确定了固定化条件、活化条件和酶的特性。在摇瓶中利用该固定化细胞进行醋酸可的松脱氢生成醋酸强的松的反应,初始底物浓度为20g/L、反应18h的转化率可达98％。在分批次反应中．适时地活化可保持固定化细胞的活性。     

2，3-丁二醇的发酵及盐析分离工艺

采用克雷伯氏菌（Klebsiella pneumoniae CICC 10011）发酵生产2,3-丁二醇,并对2,3-丁二醇的盐析分离工艺进行了考察。通过实验确定了以葡萄糖为底物微氧批式流加发酵的条件,发酵液中2,3-丁二醇和3-羟基丁酮的质量浓度分别为90．98g/L和12．40g/L,2,3-丁二醇的摩尔转化率为82．7％,生产强度达到2．1g/（L·h）。对发酵液中2,3-丁二醇的盐析分离研究表明,K2HPO4和K3PO4对2,3-丁二醇的盐析效果优于K2CO3。当发酵液浓缩70％后,加入质量分数为45％的K,HPO4,2,3-丁二醇的分配系数达到9．10,回收率为79．37％;上相中2,3-丁二醇的质量浓度达到420g／L;此时3-羟基丁酮的分配系数和回收率分别为11．9和83．48％。     

高产天冬氨酸酶的大肠杆菌细胞的固定化

用聚乙烯醇凝胶包埋具有高活力天冬氨酸酶的大肠杆菌(Escherichia coli)No.1细胞。该酶的表现活力高达1638 00u／g湿细胞,酶活力的回收率为97．5％。固定化细胞和游离细胞天冬氨酸酶的最适pH均为8．0,最适温度分别为40—45℃和40—55℃。二价金属离子Mn2+、Mg2+、Ca2+和Fe2+对热钝化的天冬氨酸酶活力具有保护作用。在37—45℃下,两种细胞的热稳定性相同。二者在pH6．0的柠檬酸缓冲液中比较稳定。固定化细胞在1mol／L、pH8．0的底物溶液(内含Mn2+1mmol／L)中于4℃冰箱保存6个月,天冬氨酸酶的活力保持不变。用固定化细胞柱连续生产L-天冬氨酸,底物转化为产物的转化率达95％以上;产物的总 收率为91．1％。固定化细胞柱连续运转40天,天冬氨酸酶活力仍保持最初酶活力的90％。     

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.     

生物催化法合成6-氰基-（3R，5R）-二羟基己酸叔丁酯

利用E.coli BL21／pCDFDuet-gdh—cr-X共表达全细胞催化6-氰基-（5R）-羟基-3-羰基己酸叔丁酯不对称还原合成6-氰基-（3R,5R）-二羟基已酸叔丁酯。结果表明：在菌体用量4．85g/L、葡萄糖与底物质量浓度比为1：1、温度28℃、pH7．0条件下,80．0g／L6-氰基-（5R）-羟基-3-羰基己酸叔丁酯生物还原2h后,底物转化率可达99．0％,产物d.e．值大于99．5％。在考察范围内,NADP^＋用量对催化效率无显著作用。     

Asymmetrical synthesis of L-homophenylalanine using engineered Escherichia coli aspartate aminotransferase

Site-directed mutagenesis was performed to change the substrate specificity of Escherichia coli aspartate aminotransferase (AAT). A double mutant, R292E/L18H, with a 12.9-fold increase in the specific activity toward L-lysine and 2-oxo-4-phenylbutanoic acid (OPBA) was identified. E. coli cells expressing this mutant enzyme could convert OPBA to L-homophenylalanine (L-HPA) with 97% yield and more than 99.9% ee using L-lysine as amino donor. The transamination product of L-lysine, 2-keto-6-aminocaproate, was cyclized nonenzymatically to form Delta(1)-piperideine 2-carboxylic acid in the reaction mixture. The low solubility of L-HPA and spontaneous cyclization of 2-keto-6-aminocaproate drove the reaction completely toward L-HPA production. This is the first aminotransferase process using L-lysine as inexpensive amino donor for the L-HPA production to be reported.     

Biotransformation of R-2-hydroxy-4-phenylbutyric acid by D-lactate dehydrogenase and Candida boidinii cells containing formate dehydrogenase coimmobilized in a fibrous bed bioreactor

R-2-hydroxy-4-phenylbutyric acid (R-HPBA) is an important intermediate in the manufacture of angiotensin converting enzyme inhibitors. In this work, a recombinant D-lactate dehydrogenase (LDH) was used to transform 2-oxo-4-phenylbutyric acid (OPBA) to R-HPBA, with concomitant oxidation of beta-nicotinamide adenine dinucleotide (NADH) to NAD(+). The cofactor NADH was regenerated by formate dehydrogenase (FDH) present in whole cells of Candida boidinii, which were pre-treated with toluene to make them permeable. The whole cells used in the process were more stable and easier to prepare as compared with the isolated FDH from the cells. Kinetic study showed that the reaction rate was dependent on the concentration of cofactor, NAD(+), and that both R-HPBA and OPBA inhibited the reaction. A novel method for co-immobilization of whole cells and LDH enzyme on cotton cloth was developed using polyethyleneimine (PEI), which induced the formation of PEI-enzyme-cell aggregates and their adsorption onto cotton cloth, leading to multilayer co-immobilization of cells and enzyme with high loading (0.5 g cell and 8 mg LDH per gram of cotton cloth) and activity yield ( > 95%). A fibrous bed bioreactor with co-immobilized cells and enzyme on the cotton cloth was then evaluated for R-HPBA production in fed-batch and repeated batch modes, which gave relatively stable reactor productivity of 9 g/L . h and product yield of 0.95 mol/mol OPBA when the concentrations of OPBA and R-HPBA were less than 10 g/L.     

L-抗坏血酸洛芬酯非水相酶促合成的动力学与热力学

对酶法合成L-抗坏血酸洛芬酯(芬维C酯)的反应动力学与热力学进行研究,确定了最有效的酶促反应环境。合成布洛芬维C酯的最优条件:转速200r/min,温度65℃,加酶量5%(以底物的质量分数计),底物浓度1mol/L,平衡所需时间66h,平衡时产物质量分数为19.07%;合成酮洛芬维C酯的最优条件:200r/min,60℃,加酶量7.5%,底物浓度600mmol/L,平衡时间132h,产物质量分数为10.63%;合成氟比洛芬维C酯的最优条件:200r/min,65℃,加酶量5%,底物浓度400mmol/L,平衡时间144h,产物质量分数为6.76%。对底物进行了比较,得到了各自的动力学与热力学参数。布洛芬米氏常数为0.101μmol/L,vmax=32.68μmol/(min.g),热力学平衡常数为0.166;酮洛芬的分别为0.144μmol/L,12.97μmol/(min.g),0.091;氟比洛芬的分别为0.185μmol/L,9.35μmol/(min.g),0.055。     

Asymmetric synthesis of L-homophenylalanine by equilibrium-shift using recombinant aromatic L-amino acid transaminase

L-Homophenylalanine (L-HPA) was asymmetrically synthesized from 2-oxo-4-phenylbutyric acid (2-OPBA) and L-aspartate using a recombinant aromatic amino acid transaminase (AroAT). To screen microorganisms having such an L-specific AroAT with a relaxed substrate inhibition in the asymmetric synthesis of unnatural amino acids, enrichment cultures were performed in a minimal media containing 50 mM L-HPA as a sole nitrogen source. To reduce the intracellular background synthetic activity by amino acid pools in the cells, a two-step screening method was used. The putative AroAT (i.e., AroATEs) from the screened Enterobacter sp. BK2K-1 was cloned, sequenced, and overexpressed in E. coli cells. The activity of the overexpressed AroATEs was 314-fold higher than that of the wild-type cell. The substrate specificities of the enzyme and homology search revealed that the cloned transaminase is true AroAT. The AroATEs showed a substrate inhibition by 2-OPBA from 40 mM in the asymmetric synthesis, which made it difficult to perform batch asymmetric synthesis of L-HPA at high concentrations of 2-OPBA. To avoid the substrate inhibition by 2-OPBA, intermittent addition of the solid-state substrate was attempted to obtain a high concentration of L-HPA. By using the cell extract (75 U) obtained from the recombinant E. coli harboring the AroATEs gene, the asymmetric synthesis of L-HPA at 840 mM of 2-OPBA resulted in >94% of conversion yield and >99% ee of L-HPA of optical purity. Due to the low solubility (<2 mM) of L-HPA in the reaction buffer, synthesized L-HPA was continuously precipitated in the reaction media, which drives the reaction equilibrium towards the product formation. After full completion of the reaction, L-HPA of high purity (>99% ee) was easily recovered by simple pH shift of the reaction media. This method can permit very efficient asymmetric synthesis of other unnatural amino acids using a single transaminase reaction.     

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。     

Continuous preparation of (S)-3-hydroxy-3-phenylpropionate by asymmetric reduction of 3-oxo-3-phenylpropionic acid ethyl ester with <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> CGMCC No.2266 in a membrane reactor

In this study, (S)-3-hydroxy-3-phenylpropionate was prepared continuously by coupling microbial transformation and membrane separation. The effect of several factors on membrane flux, reactor capacity, and reaction conversion were investigated. A kinetic model of the continuous reduction process was also developed. The appropriate molecular weight cut-off of the ultrafiltration membrane was 30 kDa. The reactor capacity reached a maximum of 0.136/h at a biomass concentration and membrane flux of 86 g/L (dry weight/reaction volume) and 20 mL/h, respectively. The (S)-3-hydroxy-3-phenylpropionate yield was 3.68 mmol/L/day after continuous reduction over seven days. The enantiometric excess of (S)-3-hydroxy-3-phenylpropionate reached above 99.5%. The kinetic constants of continuous reduction were as follows: r _m = 3.00 × 10⁻³ mol/L/h, k _cat = 3.49 × 10⁻⁴ mol/L/h, k ₁ = 3.09 × 10⁻² mol/L, and k ₂ = 5.00 × 10⁻⁷ mol/L. The kinetic model was in good agreement with the experimental data obtained during continuous reduction. Compared with batch reduction, continuous reduction can significantly improve the catalytic efficiency of microbial cells and increase the reactor capacity.     

Efficient Production of (R)-2-Hydroxy-4-Phenylbutyric Acid by Using a Coupled Reconstructed d-Lactate Dehydrogenase and Formate Dehydrogenase System

Background

(R)-2-Hydroxy-4-phenylbutyric acid [(R)-HPBA] is a key precursor for the production of angiotensin-converting enzyme inhibitors. However, the product yield and concentration of reported (R)-HPBA synthetic processes remain unsatisfactory.

Methodology/Principal Findings

The Y52L/F299Y mutant of NAD-dependent d-lactate dehydrogenase (d-nLDH) in Lactobacillus bulgaricus ATCC 11842 was found to have high bio-reduction activity toward 2-oxo-4-phenylbutyric acid (OPBA). The mutant d-nLDH^Y52L/F299Y was then coexpressed with formate dehydrogenase in Escherichia coli BL21 (DE3) to construct a novel biocatalyst E. coli DF. Thus, a novel bio-reduction process utilizing whole cells of E. coli DF as the biocatalyst and formate as the co-substrate for cofactor regeneration was developed for the production of (R)-HPBA from OPBA. The biocatalysis conditions were then optimized.

Conclusions/Significance

Under the optimum conditions, 73.4 mM OPBA was reduced to 71.8 mM (R)-HPBA in 90 min. Given its high product enantiomeric excess (>99%) and productivity (47.9 mM h⁻¹), the constructed coupling biocatalysis system is a promising alternative for (R)-HPBA production.     

葡萄酒酵母不对称还原苯甲酰甲酸合成（R）-扁桃酸

研究了葡萄酒酵母不对称还原制备（R）-扁桃酸的转化,并将其放大至反应罐进行小试研究。通过转化条件的优化,在密闭条件下,当底物质量浓度为10g/L时,苯甲酰甲酸的产率达到72％,扁桃酸的对应过量值（e.e）值达到99％以上。实验发现,该微生物具有很好的催化稳定性,全细胞经过10批次反应,产率无明显降低,产物对映体过量值均高于98％。转化反应放大至7L反应罐体系后,S.ellipsoideus,仍然具有良好的催化性能,产率提高到81％,e.e值保持在99％。