Gas phase enantioselective reduction catalyzed by immobilized ketoreductase: Effects of water activity and reaction temperature

The performance (activity, stability, enantioselectivity and productivity) of the commercial ketoreductase immobilized on non-porous glass supports was investigated as functions of the water activity and the reaction temperature in a continuous gas phase reactor. The enantioselective reduction of 2-butanone to (S)-2-butanol with the in situ regeneration of β-nicotinamide adenine dinucleotide phosphate by 2-propanol catalyzed by the immobilized ketoreductase was used as a model reaction. The activity, stability and enantioselectivity were strongly influenced by the water activity and the reaction temperature. The optimal water activity and reaction temperature were obtained at 0.8 and 313–323 K in terms of the productivity, respectively. Successfully, the enantioselectivity for the gas phase system attained the level identical to that for the aqueous phase system.     

Effect of additives on gas-phase catalysis with immobilised Thermoanaerobacter species alcohol dehydrogenase (ADH T)

This paper presents a strategy for preparing an efficient immobilised alcohol dehydrogenase preparation for a gas-phase reaction. The effects of additives such as buffers and sucrose on the immobilisation efficiency (residual activity and protein loading) and on the gas-phase reaction efficiency (initial reaction rate and half-life) of Thermoanaerobacter sp. alcohol dehydrogenase were studied. The reduction of acetophenone to 1-phenylethanol under in situ cofactor regeneration using isopropanol as co-substrate was used as a model reaction at fixed reaction conditions (temperature and thermodynamic activities). A strongly enhanced thermostability of the enzyme in the gas-phase reaction was achieved when the enzyme was immobilised with 50 mM phosphate buffer (pH 7) containing sucrose five times the protein amount (on weight/weight basis). This resulted in a remarkable productivity of 200 g L⁻¹ day⁻¹ even at non-optimised reaction conditions. The interaction of additives with the enzyme and water affects the immobilisation and gas-phase efficiencies of the enzyme. However, it was not possible to predict the effect of additives on the gas-phase reaction efficiency even after knowing their effect on the immobilisation efficiency.     

<Emphasis Type="Italic">Burkholderia cenocepacia</Emphasis>: a new biocatalyst for efficient bioreduction of ezetimibe intermediate

Ezetimibe is a selective acyl-coenzyme A: cholesterol acyltransferase (ACAT) inhibitor used in hypercholesterolemia. Synthesis of ezetimibe requires enantiopure 3-[5-(4-fluorophenyl)-5(S)-hydroxypentanoyl]-4(S)-4-phenyl-1,3-oxazolidin-2-one (FOP alcohol) as a crucial intermediate which is produced by reduction of the corresponding prochiral ketone (FOP dione). A new biocatalyst from acclimatized soil was screened for bioreduction of the above prochiral ketone. The microorganism was identified by 16S mRNA sequencing, as Burkholderia cenocepacia. Various physicochemical conditions were optimized to increase cellmass and enzyme activity. The overall increase in cellmass concentration and enzyme activity was 2.06 and 1.85-fold, respectively. Various reaction conditions, for example pH, temperature, agitation, and cellmass concentration, were optimized for maximum product yield (chiral alcohol) with excellent enantioselectivity. Best reduction was achieved in phosphate buffer (50 mM, pH 8.0) at 40°C (200 rpm) and the yield of enantiopure alcohol from the corresponding prochiral ketone was 54%. This biocatalyst was also used for the reduction of various other prochiral ketones.     

Preparation and properties of an immobilized pectinlyase for the treatment of fruit juices

Pectinlyase, present in different commercial pectinases used in juice technology, was immobilized on alginate beads. The optimal conditions were: 0.17 g alginate ml(-1), 1.2% (w/v or v/v) enzyme concentration and acetic-HCl/glycine-HCl buffer at pH 3.6 or tris-HCl/imidazole buffer at pH 6.4. Maximum percentage of immobilization (10.6%) was obtained with Rapidase C80. Kinetic parameters of free and immobilized pectinlyase were also determined. The pH and temperature at which activity of soluble and immobilized enzyme was maximum were 7.2 and 55 degrees C. Thermal stability was not significantly altered by immobilization, especially at 40 degrees C, showing two periods of different stability. Free and immobilized preparation reduced the viscosity of highly esterified pectin from 1.09 to 0.70 and 0.72 mm(2) s(-1), respectively, after 30 min at 40 degrees C. Furthermore, the immobilized enzyme could be re-used through 4 cycles and the efficiency loss in viscosity reduction was found to be only 9.2%.     

纳米磁性壳聚糖微球固定化酵母醇脱氢酶的研究

建立了以纳米级磁性壳聚糖微球(magnetic chitosan microspheres , M-CS)为载体固定化酵母醇脱氢酶(yeast alcohol dehydrogenase,YADH)的方法,优化了YADH的固定化条件,考察了固定化酶的性质。结果表明,M-CS 呈规则的圆球形,粒径在30nm 左右,具有较好的磁响应性。酵母醇脱氢酶固定化适宜条件为:50 mg 磁性壳聚糖微球,加入20mL 0.25 mg/mL 酵母醇脱氢酶(蛋白质含量)磷酸盐缓冲液(0.05 mol/L ,pH 7.0) ,在4 ℃固定2h。M-CS 容易吸附酵母醇脱氢酶,但吸附的酶量受载体与酶的比例、溶液的离子浓度、溶液pH的影响明显,而温度对吸附的酶量的影响则相对较弱。相对于游离的酵母醇脱氢酶,固定化酶的最适温度略有升高,可明显改善其热稳定性、酸碱稳定性、操作稳定性和贮存稳定性。     

Immobilization and characterization of benzoylformate decarboxylase from Pseudomonas putida on spherical silica carrier

If an adequate biocatalyst is identified for a specific reaction, immobilization is one possibility to further improve its properties. The immobilization allows easy recycling, improves the enzyme performance, and it often enhances the stability of the enzyme. In this work, the immobilization of the benzoylformate decarboxylase (BFD) variant, BFD A460I-F464I, from Pseudomonas putida was accomplished on spherical silica. Silicagel is characterized by its high mechanical stability, which allows its application in different reactor types without restrictions. The covalently bound enzyme was characterized in terms of its activity, stability, and kinetics for the formation of chiral 2-hydroxypropiophenone (2-HPP) from benzaldehyde and acetaldehyde. Moreover, temperature as well as pressure dependency of immobilized BFD A460I-F464I activity and enantioselectivity were analyzed. The used wide-pore silicagel shows a good accessibility of the immobilized enzyme. The activity of the immobilized BFD A460I-F464I variant was determined to be 70% related to the activity of the free enzyme. Thereby, the enantioselectivity of the enzyme was not influenced by the immobilization. In addition, a pressure-induced change in stereoselectivity was found both for the free and for the immobilized enzyme. With increasing pressure, the enantiomeric excess (ee) of (R)-2-HPP can be increased from 44% (0.1 MPa) to 76% (200 MPa) for the free enzyme and from 43% (0.1 MPa) to 66% (200 MPa) for the immobilized enzyme.     

Effect of immobilization support, water activity, and enzyme ionization state on cutinase activity and enantioselectivity in organic media

We studied the reaction between vinyl butyrate and 2-phenyl-1-propanol in acetonitrile catalyzed by Fusarium solani pisi cutinase immobilized on zeolites NaA and NaY and on Accurel PA-6. The choice of 2-phenyl-1-propanol was based on modeling studies that suggested moderate cutinase enantioselectivity towards this substrate. With all the supports, initial rates of transesterification were higher at a water activity (a(w)) of 0.2 than at a(w) = 0.7, and the reverse was true for initial rates of hydrolysis. By providing acid-base control in the medium through the use of solid-state buffers that control the parameter pH-pNa, which we monitored using an organo-soluble chromoionophoric indicator, we were able, in some cases, to completely eliminate dissolved butyric acid. However, none of the buffers used were able to improve the rates of transesterification relative to the blanks (no added buffer) when the enzyme was immobilized at an optimum pH of 8.5. When the enzyme was immobilized at pH 5 and exhibited only marginal activity, however, even a relatively acidic buffer with a pK(a) of 4.3 was able to restore catalytic activity to about 20% of that displayed for a pH of immobilization of 8.5, at otherwise identical conditions. As a(w) was increased from 0.2 to 0.7, rates of transesterification first increased slightly and then decreased. Rates of hydrolysis showed a steady increase in that a(w) range, and so did total initial reaction rates. The presence or absence of the buffers did not impact on the competition between transesterification and hydrolysis, regardless of whether the butyric acid formed remained as such in the reaction medium or was eliminated from the microenvironment of the enzyme through conversion into an insoluble salt. Cutinase enantioselectivity towards 2-phenyl-1-propanol was indeed low and was not affected by differences in immobilization support, enzyme protonation state, or a(w).     

Improved production of ethyl-(R)-2-hydroxy-4-phenylbutyrate with pretreated Saccharomyces cerevisiae in water/organic solvent two-liquid phase systems

Baker's yeast pretreated with α-phenacyl chloride was employed to improve the enantioselectivity of the asymmetric reduction of ethyl-2-oxo-4-phenylbutyrate (EOPB) to ethyl-(R)-2-hydroxy-4-phenylbutyrate ((R)-EHPB) and maintain a high activity of the yeast. A water/organic solvent two-liquid phase system was also introduced to overcome the strong substrate and product inhibition of the enzyme; the highest catalytic activity and enantioselectivity were obtained in a water/benzene two-liquid phase system. When the reduction was catalyzed with pretreated yeast (300 mg mL^?1 buffer) in the water/benzene two-liquid phase system (V_aq/V_ben=20:40), 41.9% molar conversion of EOPB and 87.5% e.e. of (R)-EHPB were obtained in 48 h, using pH 8.0 phosphate buffer with 1.5% (v/v) of ethanol added as a co-substrate at 30°C, even with an initial EOPB concentration of 400 mM and a final EHPB concentration as high as 167.7 mM.     

Improvement of covalent immobilization procedure of β‐galactosidase from Kluyveromyces lactis for galactooligosaccharides production: Modeling and kinetic study

Galactooligosaccharides (GOS) are prebiotics produced from lactose through an enzymatic reaction. Employing an immobilized enzyme may result in cost reductions; however, the changes in its kinetics due to immobilization has not been studied. This study experimentally determined the optimal reaction conditions for the production of GOS from lactose by β‐galactosidase (EC 3.2.1.23) from Kluyveromyces lactis covalently immobilized to a polysiloxane‐polyvinyl alcohol (POS‐PVA) polymer activated with glutaraldehyde (GA), and to study the transgalactosylation kinetics. Yield immobilization was 99 ± 1.1% with 78.5 ± 2.4% enzyme activity recovery. An experimental design 24 with 1 center point and 2 replicates was used. Factors were lactose [L], enzyme concentration [E], pH and temperature (T). Response variables were glucose and galactose as monosaccharides [G1], residual lactose [Lac]r and GOS as disaccharides [G2] and trisaccharides [G3]. Best conditions were pH 7.1, 40 °C, 270 gL^?1 initial lactose concentration and 6 U mL^?1 enzyme concentration, obtaining 25.46 ± 0.01 gL^?1 yield of trisaccharides. Although below the HPLC‐IR detection limit, tetrasaccharides were also identified after 115 min of reaction. The immobilization protocol was then optimized by diminishing total reactant volumes : support ratio, resulting in improved enzyme activity synthesizing 43.53 ± 0.02 gL^?1 of trisaccharides and 13.79 ± 0.21 gL^?1 of tetrasaccharides, and after four cycles remaining relative activity was 94%. A reaction mechanism was proposed through which a mathematical model was developed and rate constants were estimated, considering a pseudo steady‐state hypothesis for two concomitant reactions, and from this simplified analysis, the reaction yield could eventually be improved. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:1568–1578, 2017     

Comparison of physical and covalent immobilization of lipase from Candida antarctica on polyamine microspheres of alkylamine matrix

Abstract

Polyamine microspheres (PA-M) prepared using polyethyleneimine as matrix were used for the immobilization of Candida antarctica lipase. The isoelectric point of PA-M is 10.6, and the hydrophobicity of PA-M was indicated using naphthalene. Optimization of conditions showed that the maximal loading of lipase on PA-M reached 230.2 mg g^{? 1} at pH 9.0 and 35°C. An increased buffer concentration had no effect on the activity of lipase but decreased the amount of lipase adsorbed. Simulation with Langmuir and Freundlich isotherms demonstrated that the adsorption of lipase on PA-M was thermodynamically favorable. Covalent crosslinking of the lipase adsorbed extended the pH range and increased the optimal temperature of the lipase activity. The physically adsorbed lipase (P-lipase) and the covalently immobilized derivative (C-lipase) retained more than 75% and 85% of their initial activity, respectively, after 10 cycles of usage. The half-lives of P-lipase and C-lipase at 50°C were 15.70 and 27.67 times higher than that of the free enzyme, respectively. Compared to P-lipase, covalent immobilization obviously reduced the catalytic efficiency and activation energy of the enzyme.     

Optimized conditions forin situ immobilization of lipase in aldehyde-silica packed columns

Optimal conditions for thein situ immobilization of lipase in aldehyde-silica packed columns,via reductive amination, were investigated. A reactant mixture, containing lipase and sodium borohydride (NaCBH), was recirculated through an aldehyde-silica packed column, such that the covalent bonding of the lipase,via amination between the amine group of the enzyme and the aldehyde terminal of the silica, and the reduction of the resulting imine group by NaCBH, could occur inside the bed,in situ. Mobile phase conditions in the ranges of pH 7.0∼7.8, temperatures between 22∼28°C and flow rates from 0.8∼1.5 BV/min were found to be optimal for thein situ immobilization, which routinely resulted in an immobilization of more than 70 mg-lipase/g-silica. Also, the optimal ratio and concentration for feed reactants in thein situ immobilization: mass ratio [NaCBH]/[lipase] of 0.3, at NaCBH and lipase concentrations of 0.75 and 2.5 g/L, respectively, were found to display the best immobilization characteristics for concentrations of up to 80 mg-lipase/g-silica, which was more than a 2-fold increase in immobilization compared to that obtained by batch immobilization. For tributyrin hydrolysis, thein situ immobilized lipase displayed lower activity per unit mass of enzyme than the batch-immobilized or free lipase, while allowing more than a 45% increase in lipase activity per unit mass of silica compared to batch immobilization, because the quantity of the immobilization on silica was augmented by thein situ immobilization methodology used in this study.     

Optimizing Immobilization and Stabilization of Feruloyl Esterase from Humicola Insolens and its Application for the Feruloylation of Oligosaccharides

Feruloyl esterase (FAE)-catalyzed esterification reaction is as a potential route for the biosynthesis of feruloylated oligosaccharides as functional ingredients. Immobilization of FAE from Humicola insolens on metal chelate-epoxy supports was investigated. The study of effects of immobilization parameters using response surface methodology revealed the significance of enzyme/support ratio (3.25-29.25 mg/g support), immobilization time (14-38 h), buffer molarity (0.27-1.25 M) and pH (4.0-8.0). The interactions between enzyme-to-support ratio/buffer molarity and enzyme-to-support ratio/pH were found to be critical for the modulation of the immobilization activity yield and the retention of specific activity, respectively. Optimum conditions for FAE-immobilization on metal chelate Sepabeads® EC-EP R were identified to be 22.75 mg FAE/g support, pH of 5.0, 27.7 h and buffer molarity of 0.86 M. At these conditions, an activity yield of 82.4%, a specific activity retention of 143.4%, and an enzyme activity of 395.4 μmol/min. g support were achieved. Further incubation of the immobilized FAE at pH 10.0 improved its thermostability. Increasing the pore size of the epoxy support improved the retention of FAE hydrolytic activity and the esterifying efficiency of the immobilized biocatalyst. Optimally immobilized and stabilized FAE on metal chelate-epoxy support retained up to 92.9% of the free enzyme feruloylation efficiency to xylooligosaccharides..     

Highly enantioselective reduction of 4-(trimethylsilyl)-3-butyn-2-one to enantiopure (R)-4-(trimethylsilyl)-3-butyn-2-ol using a novel strain Acetobacter sp. CCTCC M209061

The biocatalytic reduction of 4-(trimethylsilyl)-3-butyn-2-one to enantiopure (R)-4-(trimethylsilyl)-3-butyn-2-ol was successfully conducted with high enantioselectivity using immobilized whole cells of a novel strain Acetobacter sp. CCTCC M209061, newly isolated from kefir. Compared with other microorganisms that were investigated, Acetobacter sp. CCTCC M209061 was shown to be more effective for the bioreduction reaction, and afforded much higher yield and product enantiomeric excess (e.e.). The optimal buffer pH, co-substrate concentration, reaction temperature, substrate concentration and shaking rate were 5.0, 130.6 mM, 30 °C, 6.0 mM and 180 r/min, respectively. Under the optimized conditions, the maximum yield and the product e.e. were 71% and >99%, respectively, which are much higher than those reported previously. Additionally, the established biocatalytic system proved to be efficient for the bioreduction of acetyltrimethylsilane to (R)-1-trimethylsilylethanol with excellent yield and product e.e. The immobilized cells manifested a good operational stability under the above reaction conditions since they retained 70% of their catalytic activity after ten cycles of use.     

树脂载体固定S-腺苷甲硫氨酸合成酶的研究

目的:筛选一种适合S-腺苷甲硫氨酸合成酶固定化的树脂载体,进行固定化工艺优化及固定化酶性质研究。方法:以固定化率和表观酶活回收率为指标,筛选固定化效果最佳的一种树脂,采用单因素实验对固定化条件进行优化。结果:阴离子交换树脂载体ESR-2表现出最优的固定化率(94.03%)和酶活回收率(47.45%);最佳固定化条件为加酶量4U/g、pH 8.0、15℃吸附10h,最佳条件下固定化酶表观酶活为2.1U/g,表观酶活回收率达51.6%。固定化酶的最适pH为8.5,最适温度为35℃,连续反应10批次后酶活剩余77.92%。结论:树脂载体ESR-2固定化S-腺苷甲硫氨酸合成酶酶活及稳定性较好,能够用于S-腺苷甲硫氨酸的工业化大规模生产。     

Resolution of N-(2-ethyl-6-methylphenyl) alanine by using microgel beads containing Pseudomonas cepacia lipase

Abstract

Pseudomonas cepacia lipase (PCL) was immobilized in alginate microgel beads by electrostatic dispersion. The high electrical potential applied in the immobilization process could significantly decrease the droplet size. The optimum conditions for lipase immobilization were 2% (w/v) alginate, 100 mM CaCl₂, 8 mg/mL enzyme, 4 kV electrical potential and 200 μm mean bead size. Under these conditions, 78.2 U/g of immobilized PCL activity was obtained with 39.1% retained activity and 57.2% immobilization efficiency. The immobilized PCL (PCL-CA) was subsequently used in the enantioselective hydrolysis of (R, S)-N-(2-ethyl-6-methylphenyl) alanine methyl ester. Although PCL-CA exhibited slightly lower activity than free PCL, it preserved the high enantioselectivity (E-value >?200), which afforded enantiomerically pure (R)-acid (99% e.e._p). Furthermore, PCL-CA exhibited higher thermal stability, storage and medium stability than that of free PCL. Batch-wise operational stability studies demonstrated that PCL-CA retained its initial activity for at least 10 cycles of hydrolysis.     

Immobilization of horseradish peroxidase onto kaolin

Kaolin showed as a very perspective carrier for the enzyme immobilization and it was used for the adsorption of horseradish peroxidase (HRP). The effects of the enzyme concentration and pH on the immobilization efficiency were studied in the reaction with pyrogallol and anthraquinone dye C.I. Acid Violet 109 (AV 109). In addition, Fourier transform infrared spectroscopy, scanning electron microscopy and analysis by Brunauer–Emmett–Teller were performed for kaolin, thermally activated kaolin and the immobilized enzyme. It has been shown that 0.1 IU of HRP-kaolin decolorized 87 % of dye solution, under the optimal conditions (pH 5.0, temperature 24 °C, dye concentration 40 mg/L and 0.2 mM of H₂O₂) within 40 min. The immobilized HRP decolorization follows the Ping Pong Bi–Bi mechanism with dead-end inhibition by the dye. The biocatalyst retained 35 ± 0.9 % of the initial activity after seven cycles of reuse in the decolorization reaction of AV 109 under optimal conditions in a batch reactor. The obtained kinetic parameters and reusability study confirmed improvement in performances of k-HRP compared to free, indicating that k-HRP has a great potential for environmental purposes.     

Purification and characterization of carbonyl reductase from Geotrichum candidum

Geotrichum candidum is well known for the reduction of prochiral ketones to chiral alcohol with high yield and excellent enantioselectivity. Carbonyl reductase from G. candidum was purified by ammonium sulphate precipitation, anion exchange and hydrophobic interaction chromatographies. Gel filtration chromatography together with SDS-PAGE revealed this protein to be a dimer of 60 kDa subunits. Maximum enzyme activity was found in acetate buffer at pH 5.4 with t_1/2 of 7.13 h at 30 °C and t_1/2 of 2.8 h at 65 °C. The enzyme was inhibited by p-hydroxymercuribenzoate and hydroxylamine indicating the involvement of thiol and carbonyl groups in the reduction reaction catalyzed by the enzyme. Chelating agents also reduced the enzyme activity indicating the requirement of metal ions as cofactors. The purified carbonyl reductase was found to be highly selective for ketones containing naphthyl ring, whereas aryl or hetero-aryl ketones showed very less or no activity at all.     

Influence of water-miscible organic solvents on kinetics and enantioselectivity of the (R)-specific alcohol dehydrogenase from Lactobacillus brevis

Using the organic solvents acetonitrile and 1,4-dioxane as water-miscible additives for the alcohol dehydrogenase (ADH)-catalyzed reduction of butan-2-one, we investigated the influence of the solvents on enzyme reaction behavior and enantioselectivity. The NADP(+)-dependent (R)-selective ADH from Lactobacillus brevis (ADH-LB) was chosen as biocatalyst. For cofactor regeneration, the substrate-coupled approach using propan-2-ol as co-substrate was applied. Acetonitrile and 1,4-dioxane were tested from mole fraction 0.015 up to 0.1. Initial rate experiments revealed a complex kinetic behavior with enzyme activation caused by the substrate butan-2-one, and increasing K(M) values with increasing solvent concentration. Furthermore, these experiments showed an enhancement of the enantioselectivity for (R)-butan-2-ol from 37% enantiomeric excess (ee) in pure phosphate buffer up to 43% ee in the presence of 0.1 mol fraction acetonitrile. Finally, the influence of the co-solvents on water activity of the reaction mixture and on enzyme stability was investigated.     

Crosslinked aggregates of Rhizopus oryzae lipase as industrial biocatalysts: Preparation, optimization, characterization, and application for enantioselective resolution reactions

Lipase from Rhizopus oryzae (ROL) was immobilized as crosslinked enzyme aggregate (CLEA) via precipitation with ammonium sulfate and simultaneous crosslinking with glutaraldehyde. The optimum conditions of the immobilization process were determined. Lipase CLEAs showed a twofold increase in activity when Tween 80‐pretreated lipase was used for CLEA preparation. CLEAs were shown to have several advantages compared to free lipase. CLEAs were more stable at 50°C and 60°C as well as for a wide range of pH. After incubation at 50°C, CLEA showed 74% of initial activity whereas free enzyme was totally inactivated. Reduction of Schiff bases has been performed for the first time in the CLEA preparation process significantly improving the chemically modified CLEAs' reusability, thus providing an enzyme with high potential for recycling even under aqueous reaction conditions where enzyme leakage is, in general, one of the major problems. The CLEA retained 91% activity after 10 cycles in aqueous medium. The immobilized enzyme was used for kinetic resolution reactions. Results showed that immobilization had an enhancing effect on the conversion (c) as well as on the enantiomeric ratio (E). ROL CLEA displayed five times higher enantioselectivity for the hydrolysis of (R,S)‐1‐phenylethyl acetate and likewise 1.5 times higher enantioselectivity for the transesterification of racemic (R–S)‐1‐phenylethanol with vinylacetate. © 2012 American Institute of Chemical Engineers Biotechnol. Prog., 28: 937–945, 2012 This article was published online on June 26, 2012. An edit was subsequently requested. This notice is included in the online and print versions to indicate that both have been corrected [27 June 2012].     

Asymmetric reduction of 3-chloropropiophenone to (S)-3-chloro-1-phenylpropanol using immobilized Saccharomyces cerevisiae CGMCC 2266 cells

(S)-3-Chloro-1-phenylpropanol is an important chiral precursor for numerous antidepressants such as tomoxetine. A high enantiomeric excess (e.e.) of (S)-3-chloro-1-phenylpropanol can be achieved by asymmetric reduction of 3-chloropropiophenone using Saccharomyces cerevisiae CGMCC 2266 cells immobilized in calcium alginate. Thermal pretreatment of the immobilized cells at 50 °C for 30 min resulted in high enantioselectivity (99% e.e.) and good percent conversion (80%). The effects of various conditions on the reduction reaction were investigated. The optimal conditions were found to be as follows: sodium alginate concentration, 2%; bead diameter, 2 mm; temperature, 30 °C; re-culture time, 24 h; and batch addition of the substrate. After reusing these three times, the immobilized cells retained approximately 60% of their original catalytic activity with their enantioselectivity intact.