Efficient production of (R)-(−)-mandelic acid in biphasic system by immobilized recombinant E. coli

The recombinant Escherichia coli M15/BCJ2315 which harbored a mandelonitrilase from Burkholderia cenocepacia J2315 was immobilized via catecholic chitosan and functionalized with magnetism by iron oxide nanoparticles. The immobilized cells showed high activity recovery, enhanced stability and good operability in the enantioselective hydrolysis of mandelonitrile to (R)-(−)-mandelic acid. Furthermore, the immobilized cells were reused up to 15 cycles without any activity loss in completely hydrolyzing mandelonitrile (100 mM) within 1 h in aqueous solution. The ethyl acetate–water biphasic system was built and optimized. Under the optimal conditions, as high as 1 M mandelonitrile could be hydrolyzed within 4 h with a final yield and ee value of 99% and 95%, respectively. Moreover, the successive hydrolysis of mandelonitrile was performed by repeated use of the immobilized cells for 6 batches, giving a final productivity (g L⁻¹ h⁻¹) and relative production (g g⁻¹) of 40.9 and 38.9, respectively.     

Production of R-(-)-mandelic acid from mandelonitrile by Alcaligenes faecalis ATCC 8750.

R-(-)-Mandelic acid was produced from racemic mandelonitrile by Alcaligenes faecalis ATCC 8750. Ammonium acetate or L-glutamic acid as the carbon source and n-butyronitrile as the inducer in the culture medium were effective for bacterial growth and the induction of R-(-)-mandelic acid-producing activity. The R-(-)-mandelic acid formed from mandelonitrile by resting cells was present in a 100% enantiomeric excess. A. faecalis ATCC 8750 has an R-enantioselective nitrilase for mandelonitrile and an amidase for mandelamide. As R-(-)-mandelic acid was produced from racemic mandelonitrile in a yield of 91%, whereas no S-mandelonitrile was left, the S-mandelonitrile remaining in the reaction is spontaneously racemized because of the chemical equilibrium and is used as the substrate. Consequently, almost all the mandelonitrile is consumed and converted to R-(-)-mandelic acid. R-(-)-Mandelic acid was also produced when benzaldehyde plus HCN was used as the substrate.     

Production of R-(-)-mandelic acid from mandelonitrile by Alcaligenes faecalis ATCC 8750.

R-(-)-Mandelic acid was produced from racemic mandelonitrile by Alcaligenes faecalis ATCC 8750. Ammonium acetate or L-glutamic acid as the carbon source and n-butyronitrile as the inducer in the culture medium were effective for bacterial growth and the induction of R-(-)-mandelic acid-producing activity. The R-(-)-mandelic acid formed from mandelonitrile by resting cells was present in a 100% enantiomeric excess. A. faecalis ATCC 8750 has an R-enantioselective nitrilase for mandelonitrile and an amidase for mandelamide. As R-(-)-mandelic acid was produced from racemic mandelonitrile in a yield of 91%, whereas no S-mandelonitrile was left, the S-mandelonitrile remaining in the reaction is spontaneously racemized because of the chemical equilibrium and is used as the substrate. Consequently, almost all the mandelonitrile is consumed and converted to R-(-)-mandelic acid. R-(-)-Mandelic acid was also produced when benzaldehyde plus HCN was used as the substrate.     

Biocatalytic synthesis of (<Emphasis Type="Italic">R</Emphasis>)-(−)-mandelic acid from racemic mandelonitrile by cetyltrimethylammonium bromide-permeabilized cells of <Emphasis Type="Italic">Alcaligenes faecalis</Emphasis> ECU0401

The nitrilase from Alcaligenes faecalis ECU0401 belongs to the category of arylacetonitrilase, which could hydrolyze 2-chloromandelonitrile, 3,4-dimethoxyphenylacetonitrile, mandelonitrile, and phenylacetonitrile into the corresponding arylacetic acids. To overcome the permeability barrier and prepare whole cell biocatalysts with high activities, permeabilization of Alcaligenes faecalis ECU0401 in relation to nitrilase activity was optimized by using cetyltrimethylammonium bromide (CTAB) as permeabilizing agent. The nitrilase activity from Alcaligenes faecalis ECU0401 increased 4.5-fold when the cells were permeabilized with 0.3% (w/v) CTAB for 20 min at 25°C and pH 6.5. Consequently, almost all the mandelonitrile was consumed and converted to (R)-(−)-mandelic acid with greater than 99.9% enantiomeric excess (e.e.) by the CTAB-permeabilized cells. The permeability barrier has been significantly reduced in the hydrolysis of mandelonitrile by using CTAB-permeabilized cells and a dynamic resolution was successfully achieved, giving a 100% theoretical yield of (R)-(−)-mandelic acid. Efficient biocatalyst recycling was achieved as a result of cell immobilization in calcium alginate, with a product-to-biocatalyst ratio of 3.82 g (R)-(−)-mandelic acid g⁻¹ dry cell weight (dcw) cell after 20 cycles of repeated use.     

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％。     

Efficient production of (R)-(−)-mandelic acid with highly substrate/product tolerant and enantioselective nitrilase of recombinant Alcaligenes sp.

For efficient production of (R)-(−)-mandelic acid, a nitrilase gene from Alcaligenes sp. ECU0401 was cloned and overexpressed in Escherichia coli. After simple optimization of the culture conditions, the biocatalyst production was greatly increased from 500 to 7000 U/l. The recombinant E. coli whole cells showed strong tolerance against a high substrate concentration of up to 200 mM, and the concentration of (R)-(−)-mandelic acid after only 4 h of transformation reached 197 mM with an enantiomeric excess (ee_p) of 99%. In a fed-batch reaction with 600 mM mandelonitrile as the substrate, the cumulative production of (R)-(−)-mandelic acid after 17.5 h of conversion reached 520 mM. The recombinant E. coli cells could also be repeatedly used in the biotransformation, retaining 40% of the initial activity after 10 batches of reaction. The highly substrate/product tolerable and enantioselective nature of this recombinant nitrilase suggests that it is of great potential for the practical production of optically pure (R)-(−)-mandelic acid.     

金属螯合载体固定重组腈水解酶

以琼脂粉为基质制备金属螯合载体,并用于固定重组腈水解酶。研究发现:制备金属螯合载体最合适的金属离子为Zn2+。当Zn2+离子浓度0.3 mol/L、给酶量15.6 mg/g、固定化pH 8.0、固定化温度40℃时,制得的固定化酶活性最高。固定化酶最适反应温度为50℃、最适反应pH为7.0。当扁桃腈浓度为10 mmol/L、反应1 h时,固定化酶最大产率为0.041 mmol/(g·h);在反应12 h时,产物e.e.值可达到99%以上。固定化酶重复使用8次以后,酶活力仍保持在45%。     

Efficient preparation of (R)-alpha-monobenzoyl glycerol by lipase catalyzed asymmetric esterification: optimization and operation in packed bed reactor

Optically active (R)-alpha-monobenzoyl glycerol (MBG) was synthesized by Candida antarctica lipase B (CHIRAZYME L-2) catalyzed asymmetric esterification of glycerol with benzoic anhydride in organic solvents. Various conditions, such as the type and composition of the organic solvent, water content of the system, reaction temperature, and concentrations of the substrates were systematically examined and optimized in screw-capped test tubes with respect to both the reaction rate and the enzyme selectivity. 1,4-Dioxane was found to be the best solvent and no additional water was needed for the system. The optimum temperature was around 30 degrees C, while the most suitable substrate concentrations were 100 mM each for glycerol and benzoic anhydride, respectively. However, when excessive anhydride (e.g., 200 mM) was used, the produced MBG could be further transformed into 1,3-dibenzoyl glycerol (DBG) by the same enzyme with a priority to (S)-MBG, resulting in a significant improvement of the product optical purity from ca. 50-70% e.e. Under optimal conditions (100 mM glycerol, 100-200 mM benzoic anhydride, dioxane, 25-30 degrees C), the enzymatic synthesis of (R)-MBG was successfully operated in a packed-bed reactor for about 1 week, with an average productivity of 0.79 g MBG/day/g biocatalyst in the case of continuous operation and 0.94 g MBG/day/g biocatalyst in the case of semicontinuous operation. After refinement and preferential crystallization of the crude product, (R)-MBG could be obtained in an almost optically pure form (>98% e.e.).     

Expanding the repertoire of nitrilases with broad substrate specificity and high substrate tolerance for biocatalytic applications

Enzymatic conversion of nitriles to carboxylic acids by nitrilases has gained significance in the green synthesis of several pharmaceutical precursors and fine chemicals. Although nitrilases from several sources have been characterized, there exists a scope for identifying broad spectrum nitrilases exhibiting higher substrate tolerance and better thermostability to develop industrially relevant biocatalytic processes. Through genome mining, we have identified nine novel nitrilase sequences from bacteria and evaluated their activity on a broad spectrum of 23 industrially relevant nitrile substrates. Nitrilases from Zobellia galactanivorans, Achromobacter insolitus and Cupriavidus necator were highly active on varying classes of nitriles and applied as whole cell biocatalysts in lab scale processes. Z. galactanivorans nitrilase could convert 4-cyanopyridine to achieve yields of 1.79 M isonicotinic acid within 3 h via fed-batch substrate addition. The nitrilase from A. insolitus could hydrolyze 630 mM iminodiacetonitrile at a fast rate, effecting 86 % conversion to iminodiacetic acid within 1 h. The arylaliphatic nitrilase from C. necator catalysed enantioselective hydrolysis of 740 mM mandelonitrile to (R)-mandelic acid in 4 h. Significantly high product yields suggest that these enzymes would be promising additions to the suite of nitrilases for upscale biocatalytic application.     

Enhancing the catalytic potential of nitrilase from Pseudomonas putida for stereoselective nitrile hydrolysis

(R)-mandelic acid was produced from racemic mandelonitrile using free and immobilized cells of Pseudomonas putida MTCC 5110 harbouring a stereoselective nitrilase. In addition to the optimization of culture conditions and medium components, an inducer feeding approach is suggested to achieve enhanced enzyme production and therefore higher degree of conversion of mandelonitrile. The relationship between cell growth periodicity and enzyme accumulation was also studied, and the addition of the inducer was delayed by 6 h to achieve maximum nitrilase activity. The nitrilase expression was also authenticated by the sodium dodecyl phosphate-polyacrylamide gel electrophoresis analysis. P. putida MTCC 5110 cells were further immobilized in calcium alginate, and the immobilized biocatalyst preparation was used for the enantioselective hydrolysis of mandelonitrile. The immobilized system was characterized based on the Thiele modulus (ϕ). Efficient biocatalyst recycling was achieved as a result of immobilization with immobilized cells exhibiting 88% conversion even after 20 batch recycles. Finally, a fed batch reaction was set up on a preparative scale to produce 1.95 g of (R)-(-)-mandelic acid with an enantiomeric excess of 98.8%.     

响应面分析法优化(R)-扁桃酸发酵培养基

采用响应面分析法对Bacillussp.HB20菌株合成(R)-扁桃酸的培养基成分进行优化。首先利用Plackett-Burman试验设计筛选出影响(R)-扁桃酸产率的三个主要因素:麦芽糖、蛋白胨和牛肉膏。在此基础上用最陡爬坡路径逼近最大响应区域,再利用Box-Behnken试验设计及响应面分析法进行回归分析。结果表明,麦芽糖、蛋白胨和牛肉膏浓度与(R)-扁桃酸产率存在显著的相关性,通过求解回归方程得到最佳质量浓度:蛋白胨11.507g/L,牛肉膏6.708g/L,麦芽糖10.907g/L,(R)-扁桃酸产率理论最大值达到66.87%。经模型验证,预测值与验证试验平均值接近,在优化条件下(R)-扁桃酸产率提高了25.87%。     

Enzymatic production of 4-hydroxyphenylacetaldehyde by oxidation of the amino group of tyramine with a recombinant primary amine oxidase

In this study, an efficient enzymatic process for the synthesis of 4-hydroxyphenylacetaldehyde (4-HPAA) from tyramine was developed using whole cells of recombinant Escherichia coli co-expressing primary amine oxidase (PrAO) from E. coli and catalase (CAT) from Bacillus pumilus. The reaction conditions for the synthesis of 4-HPAA were systematically optimized starting from a monophasic aqueous buffer. The optimum reaction temperature, pH, and biocatalyst loading were 33 °C, 7.5, and 20 g/L wet cells, respectively. Substrate feeding strategies were employed to alleviate substrate inhibition, providing a 14.8 % increase in yield. A biphasic catalytic system was explored to avoid product inhibition and thus further improve the 4-HPAA yield. Ethyl acetate was found to be the best organic solvent, and the optimum volume ratio of the organic phase to the aqueous phase was 40 % (v/v). Under the optimized conditions on a 1 L scale, a yield of 76.5 % was obtained with a substrate concentration of 120 mM. Thus, the bioconversion was more efficient in the ethyl acetate/buffer biphasic system than in the monophasic aqueous system, and the yield of 4-HPAA was improved 1.89-fold.     

Cloning and biochemical properties of a highly thermostable and enantioselective nitrilase from Alcaligenes sp. ECU0401 and its potential for (R)-(?)-mandelic acid production

A nitrilase gene from Alcaligenes sp. ECU0401 was cloned and overexpressed in Escherichia coli BL21 (DE3) in a soluble form. The encoded protein with a His₆-tag was purified to nearly homogeneity as revealed by SDS-PAGE with a molecular weight of approximately 38.5 kDa, and the holoenzyme was estimated to be composed of 10 subunits of identical size by size exclusion chromatography. The V _max and K _m parameters were determined to be 27.9 μmol min⁻¹ mg⁻¹ protein and 21.8 mM, respectively, with mandelonitrile as the substrate. The purified enzyme was highly thermostable with a half life of 155 h at 30 °C and 94 h at 40 °C. Racemic mandelonitrile (50 mM) could be enantioselectively hydrolyzed to (R)-(−)-mandelic acid by the purified nitrilase with an enantiomeric excess of 97%. The extreme stability, high activity and enantioselectivity of this nitrilase provide a solid base for its practical application in the production of (R)-(−)-mandelic acid.     

Bioconversion of p-coumaric acid to p-hydroxystyrene using phenolic acid decarboxylase from B. amyloliquefaciens in biphasic reaction system

Phenolic acid decarboxylase (PAD) catalyzes the non-oxidative decarboxylation of p-coumaric acid (pCA) to p-hydroxystyrene (pHS). PAD from Bacillus amyloliquefaciens (BAPAD), which showed k _cat/K _m value for pCA (9.3?×?10³?mM^?1?s^?1), was found as the most active one using the “Subgrouping Automata” program and by comparing enzyme activity. However, the production of pHS of recombinant Escherichia coli harboring BAPAD showed only a 22.7 % conversion yield due to product inhibition. Based on the partition coefficient of pHS and biocompatibility of the cell, 1-octanol was selected for the biphasic reaction. The conversion yield increased up to 98.0 % and 0.83 g/h/g DCW productivity was achieved at 100 mM pCA using equal volume of 1-octanol as an organic solvent. In the optimized biphasic reactor, using a three volume ratio of 1-octanol to phosphate buffer phase (50 mM, pH 7.0), the recombinant E. coli produced pHS with a 88.7 % conversion yield and 1.34 g/h/g DCW productivity at 300 mM pCA.     

Enzymatic production of 2-amino-2,3-dimethylbutyramide by cyanide-resistant nitrile hydratase

A novel enzymatic route for the synthesis of 2-amino-2,3-dimethylbutyramide (ADBA), important intermediate of highly potent and broad-spectrum imidazolinone herbicides, from 2-amino-2,3-dimethylbutyronitrile (ADBN) was developed. Strain Rhodococcus boritolerans CCTCC M 208108 harboring nitrile hydratase (NHase) towards ADBN was screened through a sophisticated colorimetric screening method and was found to be resistant to cyanide (5 mM). Resting cells of R. boritolerans CCTCC M 208108 also proved to be tolerant against high product concentration (40 g l⁻¹) and alkaline pH (pH 9.3). A preparative scale process for continuous production of ADBA in both aqueous and biphasic systems was developed and some key parameters of the biocatalytic process were optimized. Inhibition of NHase by cyanide dissociated from ADBN was successfully overcome by temperature control (at 10°C). The product concentration, yield and catalyst productivity were further improved to 50 g l⁻¹, 91% and 6.3 g product/g catalyst using a 30/70 (v/v) n-hexane/water biphasic system. Furthermore, cells of R. boritolerans CCTCC M 208108 could be reused for at lease twice by stopping the continuous reaction before cyanide concentration rose to 2 mM, with the catalyst productivity increasing to 12.3 g product/g catalyst. These results demonstrated that enzymatic synthesis of ADBA using whole cells of R. boritolerans CCTCC M 208108 showed potential for industrial application.     

Preparation of ethyl 3R,5S-6-(benzyloxy)-3,5-dihydroxy-hexanoate by recombinant diketoreductase in a biphasic system

Diketoreductase from Acinetobacter baylyi ATCC 33305 is a unique carbonyl reductase, which can stereoselectively reduce ethyl-6-(benzyloxy)-3,5-dioxohexanoate to ethyl 3R,5S-6-(benzyloxy)-3,5-dihydroxy-hexanoate, an advanced intermediate for statin drugs. In the present study, we explored an aqueous-organic biphasic reaction system to make this biocatalyst more practical and valuable. Different from most oxidoreductases, diketoreductase displayed an excellent tolerance to certain organic solvents without any changes on the catalytic properties. After optimizing reaction conditions, an aqueous-hexane (1:1) biphasic system was established for the preparation of 3R,5S-dihydroxy product by diketoreductase. This system was further scaled up to 0.5 l at a substrate concentration of 105 g/l (378 mM), and the 3R,5S-hydroxy product was obtained with a yield of 83.5% and excellent stereoselectivity (de>99.5%, ee>99.5%).     

Purification and characterization of an enantioselective arylacetonitrilase from Pseudomonas putida

The highly enantioselective arylacetonitrilase of Pseudomonas putida was purified to homogeneity using a combination of (NH₄)₂SO₄ fractionation and different chromatographic techniques. The enzyme has a molecular weight of 412 kDa and consisted of approximately nine to ten identical subunits (43 kDa). The purified enzyme exhibited a pH optimum of 7.0 and temperature optimum of 40°C. The nitrilase was highly susceptible to thiol-specific reagents and metal ions and also required a reducing environment for its activity. These reflected the presence of a catalytically essential thiol group for enzyme activity which is in accordance with the proposed mechanism for nitrilase-catalyzed reaction. The enzyme was highly specific for arylacetonitriles with phenylacetonitrile and its derivatives being the most preferred substrates. Higher specificity constant (k _cat/K _m) values for phenylacetonitrile compared to mandelonitrile also revealed the same. Faster reaction rate achieved with this nitrilase for mandelonitrile hydrolysis was possibly due to the low activation energy required by the protein. Incorporation of low concentration (<5%) of organic solvent increased the enzyme activity by increasing the availability of the substrate. Higher stability of the enzyme at slightly alkaline pH and ambient temperature provides an excellent opportunity to establish a dynamic kinetic resolution process for the production of (R)-(−)-mandelic acid from readily available mandelonitrile.     

Resolution of rac-ketoprofen esters by enzymatic reactions in organic media

Enzyme-catalyzed reactions in organic media of rac-ketoprofen esters with different nucleophiles such as alcohols, amines, and water have been studied. Among the parameters optimized are the enzyme, the activated substrate, and the solvent. With the enzymes used in this study the preferred substrate was the trifluoroethyl ester of rac-ketoprofen (rac- 2 ), whose (R)-enantiomer reacted preferentially. The enzyme of choice was the lipase M-AP-10 from Mucor miehei and best results were obtained with diisopropyl ether as solvent. Three different methods have been scaled-up for the resolution of 75–150 g of substrate: transesterification with 1-butanol (90% yield of (S)-ketoprofen, 88% ee), transesterification with 2-(2-pyridyl)ethanol (94% yield, 92% ee), and hydrolysis in wet organic solvent (93% yield, 97% ee). Despite the comparable chemical and optical yields obtained with these three methods, the use of 2-(2-pyridyl)ethanol and the hydrolysis allowed a much easier work-up and isolation of the desired (+)-(S)-ketoprofen. © 1993 Wiley-Liss, Inc.     

Efficient production of (R)-o-chloromandelic acid by deracemization of o-chloromandelonitrile with a new nitrilase mined from Labrenzia aggregata

(R)-o-Chloromandelic acid is the key precursor for the synthesis of Clopidogrel?, a best-selling cardiovascular drug. Although nitrilases are often used as an efficient tool in the production of α-hydroxy acids, there is no practical nitrilase specifically developed for (R)-o-chloromandelic acid. In this work, a new nitrilase from Labrenzia aggregata (LaN) was discovered for the first time by genomic data mining, which hydrolyzed o-chloromandelonitrile with high enantioselectivity, yielding (R)-o-chloromandelic acid in 96.5% ee. The LaN was overexpressed in Escherichia coli BL21 (DE3), purified, and its catalytic properties were studied. When o-chloromandelonitrile was used as the substrate, the V(max) and K(m) of LaN were 2.53 μmol min?1 mg?1 protein and 0.39 mM, respectively, indicating its high catalytic efficiency. In addition, a study of substrate spectrum showed that LaN prefers to hydrolyze arylacetonitriles. To relieve the substrate inhibition and to improve the productivity of LaN, a biphasic system of toluene-water (1:9, v/v) was adopted, in which o-chloromandelonitrile of 300 mM (apparent concentration, based on total volume) could be transformed by LaN in 8 h, giving an isolated yield of 94.5%. The development of LaN makes it possible to produce (R)-o-chloromandelic acid by deracemizing o-chloromandelonitrile with good ee value and high substrate concentration.     

Improved production of (R)-2-octanol via asymmetric reduction of 2-octanone with Oenococcus oeni CECT4730 in a biphasic system

Abstract

Oenococcus oeni CECT4730, which catalyses the asymmetric reduction of 2-octanone to (R)-2-octanol with high enantioselectivity, was further studied to exploit its potential for production of (R)-2-octanol in an aqueous/organic solvent biphasic system. Variables such as the volume ratio of aqueous to organic phase (V_a/V_o), buffer pH, reaction temperature, shaking speed, co-substrates and the ratio of biocatalyst to substrate were examined with respect to the molar conversion, the initial reaction rate and the product enantiomeric excess (e.e.). Under the optimized conditions (V_a/V_o=1:1 (v/v), buffer pH=8.0, reaction temperature=30°C, shaking speed=150 rev/min, ratio of glucose to biomass=5.4:l (w/w), ratio of biocatalyst to substrate=0.51:l (g/mol)), the highest space time yield of (R)-2-octanol, 24 mmol L^?1 per h, and >98% product e.e. were obtained at a substrate concentration close to 1.0 mol L^?1 after 24 h reduction.