Synthesis of structured lipid with balanced omega-3: Omega-6 ratio by lipase-catalyzed acidolysis reaction: Optimization of reaction using response surface methodology

The present study deals with the production of structured lipid containing omega-3 and omega-6 fatty acids in the ratio of 1:1 by incorporating omega-3 fatty acids (α-linolenic acid) from linseed oil into groundnut oil using lipase (Lipozyme IM from Rhizomucor miehei) catalyzed acidolysis reaction in hexane. The reaction conditions were optimized by response surface methodology with a four-variable five-level central composite rotatable experimental design. The influence of four independent parameters, namely ratio of fatty acid concentrate from linseed to groundnut oil (0.66–1.98, w/w), reaction temperature (30–60 °C), enzyme concentration (1–5%) and reaction time (2–54 h) on omega-3 fatty acids incorporation into groundnut oil were optimized. Optimal conditions for the structured lipid containing omega-3 to omega-6 fatty acids in the ratio of 1:1 were determined to be; enzyme concentration 3.75% (w/w), temperature 37.5 °C, incubation time 30.81 h and ratio of free fatty acid concentrate from linseed oil to groundnut oil 1.16 (w/w).     

Immobilisation of Pseudomonas gessardii acidic lipase derived from beef tallow onto mesoporous activated carbon and its application on hydrolysis of olive oil

The study was carried out to immobilise the acidic lipase derived from Pseudomonas gessardii onto mesoporous activated carbon (MAC₄₀₀) for the application of hydrolysis of olive oil. MAC₄₀₀ was prepared from rice husk by the two stages process. P. gessardii was isolated from the beef tallow acclimatised soil. The acidic lipase (ALIP) was produced from a slaughterhouse waste, namely beef tallow as a substrate and immobilised onto MAC₄₀₀. The maximum immobilisation capacity of the MAC₄₀₀ was 3570 U/g at optimum immobilisation conditions; time (180 min), pH (5.0) and temperature (30 °C). The immobilised lipase had better thermal stability and reusability than the free lipase. The immobilisation of ALIP onto MAC₄₀₀ (MAC₄₀₀–ALIP) followed pseudo-first-order rate kinetics with rate constant 0.012/min. The Michaelis–Menten constant of MAC₄₀₀–ALIP was lower than that of the ALIP, which confirmed the higher affinity between enzyme and substrate. The immobilization of acidic lipase onto MAC₄₀₀ was confirmed by Fourier transform-infrared spectroscopy (FT-IR), scanning electron microscopy (SEM) and X-ray diffraction (XRD) pattern analysis. Reusability study of MAC₄₀₀–ALIP on olive oil hydrolysis showed 82% of hydrolysis up to 13 runs and 50% of hydrolysis up to 35 cycles of reuse. This work concludes that the acidic lipase immobilised mesoporous activated carbon matrix can be considered as a potential biocatalyst for the hydrolysis of olive oil. Thus, the enzyme immobilised matrix has potential industrial applications.”     

Immobilization of porcine pancreatic lipase on poly-hydroxybutyrate particles for the production of ethyl esters from macaw palm oils and pineapple flavor

Poly-hydroxybutyrate particles (PHB) were used as support to immobilize porcine pancreatic lipase (PPL). The biocatalysts prepared were tested in the synthesis of pineapple flavor by esterification of butanol and butyric acid in heptane medium, and in the synthesis of ethyl esters by transesterification of macaw palm pulp (MPPO) and macaw palm kernel (MPKO) oils with ethanol in solvent-free systems. The effect of protein loading on the biocatalyst activity was assessed in olive oil hydrolysis. Maximum hydrolytic activity of 292.8 ± 8.60 IU/g was observed. Langmuir isotherm model was applicable to the adsorption of PPL on PHB particles. Maximum immobilized protein amount was 24.3 ± 1.70 mg/g. The optimal pH and temperature in hydrolysis reaction for the immobilized PPL were at pH 8.5 and 50 °C, while for the crude PPL extract were at pH 8.0 and 45 °C. Immobilized PPL exhibited full hydrolytic activity after 2 h of incubation in non-polar solvents. In esterification reaction, optimal conversion was around 93% after 2 h of reaction. After six esterification cycles, the biocatalyst retained 63% of its initial activity. The biocatalyst prepared attained transesterification yield of 50% after 48 h of reaction for MPKO and 35% after 96 h of reaction for MPPO.     

Enhancing the activity and thermostability of thermostable β-glucosidase from a marine Aspergillus niger at high salinity

To evaluate the effect of salinity on the catalyzing ability of β-glucosidase in the marine fungus Aspergillus niger, the thermodynamic parameters of the β-glucosidase were investigated at different salinities. At the optimum salinity of 6% NaCl (w/v) solution, the optimum temperature and pH of the β-glucosidase activity was 66 °C and 5.0, respectively. Under these conditions, the β-glucosidase activity increased 1.46 fold. The half-life of denaturation in 6% NaCl (w/v) solution was approximately twice as long as that in NaCl free solution. The Gibb's free energy for denaturation, ΔG, was 2 kJ/mol higher in 6% NaCl (w/v) solution than in NaCl free solution. The melting point (68.51 °C) in 6% NaCl (w/v) solution was 1.71 °C higher than that (66.80 °C) in NaCl free solution. Similarly, the activity and thermostability of the pure β-glucosidase increased remarkably at high salinity. The thermostable β-glucosidase, of which the activity and the thermostability are remarkably enhanced at high salinity, is valuable for industrial hydrolyzation of cellulose in high salinity environments.     

Crosslinking of enzyme coaggregate with polyethyleneimine: A simple and promising method for preparing stable biocatalyst of Serratia marcescens lipase

Crosslinking of enzyme aggregates is a promising method for enzyme immobilization. In this work, crosslinked enzyme coaggregates of Serratia marcescens lipase with polyethyleneimine (CLECAs-SML-PEI) were prepared using polyethyleneimine (PEI) as coprecipitant and glutaraldehyde as crosslinking reagent. The crude lipase solution at a low protein concentration (0.1 mg/ml), with PEI at a mass ratio of 3:1 (PEI/protein, w/w), was found to be most adequate for the coprecipitation of SML. After crosslinking of the coaggregate of SML-PEI with 0.2% (w/v) glutaraldehyde under ambient temperature, over 70% of the total lipase activity was recovered. Compared with the free SML, the optimum temperature of the CLECAs-SML-PEI was enhanced from 50 °C to 60 °C and its thermal stability was also significantly improved. CLECAs-SML-PEI showed excellent operational stability in repeated use in aqueous–toluene biphasic system for asymmetric hydrolysis of trans-3-(4′-methoxyphenyl)glycidic acid methyl ester (MPGM), without significant inactivation after 10 rounds of repeated use.     

Hydrolysis of palm and olive oils by immobilised lipase using hollow fibre reactor

Lipase from Mucor miehei immobilised by adsorption on microporous, asymmetric hollow fibre membrane reactors was used to hydrolyse two different oils, namely, palm and olive oils. The hydrolysis reaction was carried out at a temperature of 40 °C, an average transmembrane pressure (TMP) of 115 mmHg and oil and aqueous flow rates of 2.5 and 3.0 ml min⁻¹, respectively. It was experimentally proven that adsorption of lipase increased with temperature and was higher on hydrophobic membranes than hydrophilic ones. The effluent concentrations of fatty acid products were measured using gas chromatograph with FID detector. Hydrolysis experimental results were fitted to a multisubstrate kinetic model derived from the Ping Pong Bi Bi mechanism. The final model expression is useful for predicting the free fatty acid profile of the enzymatic hydrolysis of palm and olive oils for different substrate flow rates and enzyme loading.     

1,3‐Regiospecific ethanolysis of soybean oil catalyzed by crosslinked porcine pancreas lipase aggregates

The preparation of crosslinked aggregates of pancreatic porcine lipase (PPL‐CLEA) was systematically studied, evaluating the influence of three precipitants and two crosslinking agents, as well as the use of soy protein as an alternative feeder protein on the catalytic properties and stability of the immobilized PPL. Standard CLEAs showed a global yield (CLEA’ observed activity/offered total activity) of less than 4%, whereas with the addition of soy protein (PPL:soy protein mass ratio of 1:3) the global yield was approximately fivefold higher. The CLEA of PPL prepared with soy protein as feeder (PPL:soy protein mass ratio of 1:3) and glutaraldehyde as crosslinking reagent (10 μmol of aldehyde groups/mg of total protein) was more active mainly because of the reduced enzyme leaching in the washing step. This CLEA, named PPL‐SOY‐CLEA, had an immobilization yield around 60% and an expressed activity around 40%. In the ethanolysis of soybean oil, the PPL‐SOY‐CLEA yielded maximum fatty acid ethyl ester (FAEE) concentration around 12‐fold higher than that achieved using soluble PPL (34 h reaction at 30°C, 300 rpm stirring, soybean oil/ethanol molar ratio of 1:5) with an enzyme load around 2‐fold lower (very likely due to free enzyme inactivation). The operational stability of the PPL‐SOY‐CLEA in the ethanolysis of soybean oil in a vortex flow type reactor showed that FAEE yield was higher than 50% during ten reaction cycles of 24 h. This reactor configuration may be an attractive alternative to the conventional stirred reactors for biotransformations in industrial plants using carrier‐free biocatalysts. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:910–920, 2018     

Esterification and transesterification reactions catalysed by addition of fermented solids to organic reaction media

We report for the first time both the production of the lipase of Burkholderia cepacia in solid-state fermentation and the biocatalysis of esterification and transesterification reactions through the direct addition of the lyophilised fermented solids to organic reaction media. B. cepacia produced a lipolytic activity equivalent to 108 U of pNPP-hydrolysing activity per gram of dry solids after 72 h growth on corn bran with 5% (v/w) commercial corn oil as the inducer. The fermented solid material was lyophilised and added directly to the reaction medium in esterification and transesterification reactions. A factorial design was used to study the effects on esterification of temperature, alcohol-to-acid molar ratio and amount of lipolytic activity added. All three variables affected the ester yield significantly, with the amount of enzyme being most important. A 94% ester yield was obtained at 18 h at 37 °C, with an alcohol-to-acid molar ratio of 5:1 and 60 U of added lipolytic activity. For the transesterification reaction, a factorial design was undertaken with the variables being the alcohol-to-acid molar ratio and the added lipolytic activity. Ester yields of over 95% were obtained after 120 h. Our results suggest that biocatalysis using direct addition of fermented solids to organic reaction medium should be further explored.     

Gallic acid interference on polyphenolic amperometric biosensing using Trametes versicolor laccase

The present work reports the gallic acid (GA) interference on polyphenolic amperometric biosensing using Trametes versicolor laccase (TvLac). GA′ inhibitory effect on TvLac activity was investigated on the oxidation of caffeic acid (CA) by free TvLac and its immobilised form on modified polyethersulfone membrane (PES/TvLac), using spectrophotometric and amperometric biosensor detection methods. The results have indicated that GA presents inhibitory behaviour on TvLac activity in a concentration-dependent manner. The GA concentration leading to 50% activity lost, IC₅₀, was determined to be 19.15 ± 0.11 μM and 5.11 ± 0.19 μM for free and immobilised enzyme, respectively. The results have also shown that GA exhibited a competitive and a mixed inhibition types on the TvLac activity for spectrophotometric and amperometric biosensor methods, respectively. Further GA′ and CA′ cyclic voltammetry studies have demonstrated that GA′ oxidation products interfered with CA′ redox reaction products. In fact, a decrease of the reduction current was observed at cyclic voltammograms of CA, when mixed with GA. Therefore, the GA′ interference on polyphenolic amperometric biosensing is the result of the combination of two factors: on one hand, we have the inhibitory enzymatic effect, and on the other, the reaction of GA′ oxidation products with the o-quinones obtained by the enzymatic oxidation of CA. Both gave rise to the amperometric signal decreasing effect.     

Congo Red attached monosize poly(HEMA-co-MMA) microspheres for use in reversible enzyme immobilisation

Monosize and non-porous poly(2-hydroxyethylmethacrylate-co-methylmethacrylate) (poly(HEMA-co-MMA)), microspheres were prepared by dispersion polymerisation of HEMA and MMA in an ethanol–water medium in the presence of an initiator (α,α′-azobisisobutyronitrile, AIBN). An affinity dye, i.e. Congo Red (CR) was attached covalently and then Fe³⁺ ions were incorporated. The poly(HEMA-co-MMA)-CR attached and poly(HEMA-co-MMA)-CR-Fe³⁺ incorporated microspheres were used in the immobilisation of glucose oxidase (GOD) via adsorption. The adsorption capacities of these microspheres were determined by varying the concentration of GOD in the adsorption medium. GOD adsorption capacities of the Fe³⁺ incorporated microspheres (165 mg g⁻¹) was greater than that of the dye-attached microspheres (126 mg g⁻¹). The non-specific adsorption of the GOD on the poly(HEMA-co-MMA) microspheres was negligible. The K_m values for both immobilised poly(HEMA-co-MMA)-CR-GOD (7.2) and poly(HEMA-co-MMA)-CR-Fe³⁺-GOD (6.8) were higher than that of the free enzyme (6.6 mM). Optimum reaction pH was 5.0 for free and 7.0 for both immobilised preparations. Optimum reaction temperature of the adsorbed enzymes was 10 °C higher than that of the free enzyme and was significantly broader. After 10 successive uses the retained activity of the adsorbed enzyme was 93%. It was observed that enzyme could be repeatedly adsorbed and desorbed on the CR attached poly(HEMA-co-MMA) microspheres without significant loss in adsorption capacity or enzyme activity.     

Ultrasound assisted lipase catalysed synthesis of isoamyl butyrate

The present work illustrates the incorporation of ultrasound and its improved impact in the lipase catalysed esterification. Synthesis of isoamyl butyrate from isoamyl alcohol and butyric acid using immobilised Novozym 435, has been carried out in the presence of ultrasound. The optimisation of various parameters affecting the synthesis of ester in presence of ultrasound was done. The systematic experimentation involves change of one working parameter at one time while keeping the others constant. For the maximum conversion, optimum parameters such as the ultrasound of 25 kHz frequency with power of 70 W, at the temperature of 60 °C with stirring speed of 80 rpm, mole ratio of alcohol:acid followed as 2:1, use of molecular sieves weighing 2 g, with immobilised enzyme loading of 2% (m/v) and duty cycle of 83%, were obtained. The optimum parameters collectively, gave 96% conversion of the product in 3 h as compared with 10 h in absence of ultrasound. The immobilised biocatalyst, Novozym 435 has an added benefit of reusability till 7 repetitive cycles. Besides, the synthesis is executed in the solvent free system that contributes the production of flavour in greener way.     

Towards a commercially potential process: Enzymatic recovery of phytosterols from plant oil deodoriser distillates mixture

In order to examine the industrial potential to indirectly isolate phytosterols from deodoriser distillates (DODs), enzymatic transesterification of an industrial rapeseed and soybean oil DOD mixture with bioethanol was investigated using commercial lipases and a few newly immobilised preparations of lipases. The lipases from different sources and differing preparation forms were evaluated, in terms of thermostability, enzyme efficiency, and toleration of ethanol. Lipozyme 435 and Lipozyme NS-40044 TLL were found to be most effective biocatalysts in catalysing ethanolysis of glycerides and steryl esters from DODs. The optimum conditions are 10% enzyme load (wt% of DODs), ethanol/DODs of 3.0:1.0 (mol/mol), water content 0.125% (based on the weight of total mixture), and reaction at 30 °C for 5 h. The results demonstrated that >95% sterols can be recovered as free form (>85% sterol esters were liberated as free sterols within 4 h). With this process, the system was simplified as fatty acid ethyl esters and free sterol as major components, where free sterols can be recovered via solvent extraction or molecular distillation. Furthermore, a reuse study of enzyme in consecutive batch reactions demonstrated an excellent operation stability and reusability of Lipozyme 435 and Lipozyme NS-40044 TLL with the developed process. This work indicated that the industrially refined waste DODs can be directly subjected to an enzymatic process for high efficacy recovery of phytosterol without any pre-process, driven by robust lipase preparations.     

Effective technological pectinases by Aspergillus carneus NRC1 utilizing the Egyptian orange juice industry scraps

The production of a notable and highly effective pectinase by the local fungal strain Aspergillus carneus NRC1 utilizing the abundant Egyptian orange peels and pulps (OPP) scraps excluded in the orange juice and canning industry was achieved in 5-day submerged fermentation (SMF) cultures, at temperature and pH ranges of 30–55 °C and 5.0–5.5, respectively. Fresh or thawed OPP (6%, w/v) were the most preferable sole carbon source. Pectinase activity was dramatically stimulated by ammonium sulphate as the sole nitrogen source, and at the same time strongly inhibited the production of the other tested enzymes, i.e., cellulases and hemicellulases. The lyophilized enzyme preparation was free from any ochra or aflatoxins. The optimum conditions of this methodology including enzyme and substrate (citrus pectin) concentrations were 40 mg ml^?1 and 7% (w/v), respectively, with pH and temperature of 4.0 and 55 °C, respectively.     

Hen egg white as a feeder protein for lipase immobilization

Enzyme stabilization via immobilization is one of the preferred processes as it provides the advantages of recovery and reusability. In this study, Thermomyces lanuginosus lipase has been immobilized through crosslinking using 2% glutaraldehyde and hen egg white, as an approach towards CLEA preparation. The immobilization efficiency and the properties of the immobilized enzyme in terms of stability to pH, temperature, and denaturants was studied and compared with the free enzyme. Immobilization efficiency of 56% was achieved with hen egg white. The immobilized enzyme displayed a shift in optimum pH towards the acidic side with an optimum at pH 4.0 whereas the pH optimum for free enzyme was at pH 6.0. The immobilized enzyme was stable at higher temperature retaining about 83% of its maximum activity as compared to the free enzyme retaining only 41% activity at 70 °C. The denaturation of lipase in free form was rapid with a half-life of 2 h at 60 °C and 58 min at 70 °C as compared to 12 h at 60 °C and 2 h at 70 °C for the immobilized enzyme. The effect of denaturants, urea and guanidine hydrochloride on the free and immobilized enzyme was studied and the immobilized enzyme was found to be more stable towards denaturants retaining 74% activity in 8 M urea and 98% in 6 M GndHCl as compared to 42% and 33% respectively in the case of free enzyme. The apparent K_m (2.08 mM) and apparent V_max (0.95 μmol/min) of immobilized enzyme was lower as compared to free enzyme; K_m (8.0 mM) and V_max (2.857 μmol/min). The immobilized enzyme was reused several times for the hydrolysis of olive oil.     

Immobilized lipase on macroporous polystyrene modified by PAMAM-dendrimer and their enzymatic hydrolysis

The novel enzyme carrier, polyamidoamine (PAMAM) dendrimers modified macroporous polystyrene, has been synthesized by Michael addition and firstly used in the immobilization of porcine pancreas lipase (PPL) effectively by covalent attachment. The resulting carrier was characterized with the Fourier transform infrared spectra (FT-IR), scanning electron microscopy (SEM), elemental analysis and thermogravimetric (TG) analysis. Meanwhile, the amount of immobilized lipase was up to 100 mg g⁻¹ support and the factors related with the enzyme activity were investigated. The immobilization of the PPL improved their performance in wider ranges of pH and temperature. Thermal stability of the immobilized lipase also increased dramatically in comparison with the free ones and the immobilized lipase exhibited a favorable denaturant tolerance. As a biocatalyst, the immobilized lipase for batch hydrolysis of olive oil emulsion retained 85% activity after 10 times of recycling. This well-reusability of immobilized lipase was very valuable and meaningful in enzyme technology.     

Lipase catalyzed preparation of biodiesel from Jatropha oil in a solvent free system

The monoethyl esters of the long chain fatty acids (biodiesel) were prepared by alcoholysis of Jatropha oil, a non-edible oil, by a lipase. The process optimization consisted of (a) screening of various commercial lipase preparations, (b) pH tuning, (c) immobilization, (d) varying water content in the reaction media, (e) varying amount of enzyme used, and (f) varying temperature of the reaction. The best yield 98% (w/w) was obtained by using Pseudomonas cepacia lipase immobilized on celite at 50 °C in the presence of 4–5% (w/w) water in 8 h. It was found that yields were not affected if analytical grade alcohol was replaced by commercial grade alcohol. This biocatalyst could be used four times without loss of any activity.     

Reactivity improvement of cellulolytic enzyme lignin via mild hydrothermal modification

Isolated by the cellulolytic enzyme lignin (CEL) process, water-alcohol (1:1, v/v) was introduced as co-solvent in the process of the hydrothermal treatment. The modification parameters such as reaction temperature and time, solid-to-liquid ratio, and catalysts (NaOH and NaOAlO₂) have been investigated in terms of the specific lignin properties, such as the phenolic hydroxyl content (OH_phen), DPPH free radical scavenging rate, and formaldehyde value. The CELs were also characterized by GPC, FT-IR and ¹ H NMR spectroscopy, and Py-GC/MS. The key data are under optimal lignin modification conditions (solid-to-liquid ratio of 1:10 (w/v) and a temperature of 250 °C for 60 min) are: OH_phen content: 2.50 mmol/g; half maximal inhibitory concentration (IC₅₀) towards DPPH free radicals: 88.2 mg/L; formaldehyde value: 446.9 g/kg). Both base catalysts decrease the residue rate, but phenol reactivities of the products were also detracted. Py-GC/MS results revealed that modified lignin had a higher phenolic composition than the CEL did, especially the modified lignin without catalyst (ML), which represented 74.51% phenolic content.     

Preparation of a diacylglycerol-enriched soybean oil by phosphalipase A1 catalyzed hydrolysis

Partial hydrolysis catalyzed by phospholipase A1 (Lecitase Ultra) in a solvent free system was firstly used to produce diacylglycerols (DAGs)-enriched soybean oil. In this study, five reaction parameters namely agitation speed (100–500 rpm), reaction time (2–10 h), water content (10–50 wt% of oil mass), enzyme load (5–40 U/g of oil mass), and reaction temperature (30–70 °C) were investigated. The reaction was up-scaled to 1 kg of soybean oil at 40 °C of reaction temperature, with 300 rpm of agitation speed, 40 wt% of water content, 6 h of reaction time and 22 U/g of enzyme load. Purification by molecular distillation yielded 70% DAG-enriched oil with 42.64 wt% of DAG. The composition of acylglycerols of soybean oil and the DAG-enriched soybean oil was analyzed and identified by high performance liquid chromatography (HPLC) and HPLC/electrospray ionization/mass spectrometer. The released fatty acid from the partial hydrolysis of soybean oil catalyzed by phospholipase A1 showed a higher saturated fatty acid content than that of the raw material. Compared to the lipase catalyzed process, this new phospholipase A1 catalyzed one showed the advantages of low amount production of byproduct, namely, monoacylglycerols.     

Synthesis of cellobiose-containing oligosaccharides by intermolecular transglucosylation of cyclodextrin glycosyltransferase from Paenibacillus sp. A11

Intermolecular transglucosylation of cyclodextrin glycosyltransferase (CGTase) was investigated for its use in oligosaccharide synthesis. From the kinetic parameters of the CGTase-catalyzed transglucosylation reaction, using β-cyclodextrin (β-CD) as the glucosyl donor and various saccharides or derivatives as acceptors, the efficient acceptors of the Paenibacillus sp. A11 enzyme were glucose, sorbose, lactose and cellobiose. Amongst these acceptors, cellobiose showed the highest k_cat/K_m value. The transglucosylation yields of the reactions for cellobiose, sorbose and glucose acceptors were 78, 57 and 54%, respectively, making cellobiose the most efficient acceptor of the tested saccharides in coupling with β-CD. The optimal condition for the coupling reaction was determined as: 2% (w/v) β-CD and 0.5% (w/v) cellobiose, incubated with 64 U/mL of CGTase at 30 °C for 2 h. Two main transfer products detected by HPLC, PC1 and PC2, with retention times of 3.81 and 4.42 min, respectively, and a product ratio of 3:1, had a molecular mass of 504 and 666 Da, respectively, as analyzed by mass spectrometry. The structures suggested by NMR were a trisaccharide and a novel tetrasaccharide-containing cellobiose of the structures glc (α1 → 4) glc (β1 → 4) glc and glc (α1 → 4) glc (α1 → 4) glc (β1 → 4) glc, respectively. The products were found to be resistant to hydrolysis by α-amylase.     

Enantioselective reduction of aryl ketones using immobilized cells of Candida viswanathii

Enantioselective reduction of 1-acetonapthone to S(−)-1-(1-naphthyl) ethanol, a key intermediate for the synthesis of HMG Co-A reductase inhibitor, was successfully carried out using immobilized cells of a newly isolated carbonyl reductase producing yeast strain Candida viswanathii MTCC 5158. Calcium alginate (1.5%, w/v) gave the best immobilization efficiency. Among different organic solvents and ionic liquids tried as reaction media, isopropanol gave the best enantioselectivity with moderate conversion. The immobilized cells (100 mg/ml in 50 mM Tris buffer pH 9) showed best results at a substrate concentration of 0.2 mg/ml at 30 °C. After twelve cycles of reaction, no significant decrease in bioreduction efficiency of the immobilized cells was observed as compared to the free cells.