Simple strategy of reactivation of a partially inactivated penicillin g acylase biocatalyst in organic solvent and its impact on the synthesis of β‐lactam antibiotics

Some reactions of organic synthesis require to be performed in rather aggressive media, like organic solvents, that frequently impair enzyme operational stability to a considerable extent. We have studied the option of developing a reactivation strategy to increase biocatalyst lifespan under such conditions, under the hypothesis that organic solvent enzyme inactivation is a reversible process. Glyoxyl agarose immobilized penicillin G acylase and cross‐linked enzyme aggregates of the enzyme were considered as biocatalysts performing in dioxane medium. Reactivation strategy consisted in re‐incubation in aqueous medium of the partly inactivated biocatalysts in organic medium, best conditions of reactivation being studied with respect to dioxane concentration and level of enzyme inactivation attained prior to reactivation. Best results were obtained with glyoxyl agarose immobilized penicillin G acylase at all levels of residual activity studied, with reactivations up to 50%; for the case of a biocatalyst inactivated down to 75% of its initial activity, full recovery of enzyme activity was obtained after reactivation. The potential of this strategy was evaluated in the thermodynamically controlled synthesis of deacetoxycephalosporin G in a sequential batch reactor operation, where a 20% increase in the cumulative productivity was obtained by including an intermediate stage of reactivation after 50% inactivation. Biotechnol. Bioeng. 2009;103: 472–479. © 2009 Wiley Periodicals, Inc.     

Some properties of a papain–agarose reactor provided with a pH monitor

A small reactor of immobilized papain was used to gain some knowledge about the effect of immobilization upon the reactivity of the enzyme towards one substrate and various types of inhibitors. A buffer solution containing benzoyl–arginine ethyl ester as substrate was run through a small column of papain immobilized by attachment to agarose beads. The pH of the effluent was measured continuously and provided the data used to calculate the substrate conversion during passage through the reactor. The operation of the system was checked by determining the substrate conversion as a function of flow rate. It proved to operate as theory demanded. The rate and extent of inhibition were measured after addition of various inhibitors to the buffer–substrate solution. The following quantities of immobilized papain were found to be equal within ±20% to those of the free enzyme in solution: the overall activity, the K_m of benzoyl–arginine ethyl ester, the K_i of the competitive inhibitor benzoylamino-acetonitrile, the rate of inactivation by chloroacetic acid and by chloroacetamide, the rate of activation by cysteine of the mixed disulfide of papain and cysteine, and the rate of spontaneous reactivation of the KCNO–papain adduct. The inactivation by KCNO proved to be strongly pH dependent. This may explain why the rate of the latter reaction is only 66% of the rate with free enzyme. It is concluded that the rates and equilibrium constants measured in the present reactor system are within ±20% of the values of the dissolved enzyme, provided that the reactions are not strongly pH dependent. Calculation showed there was no diffusion limitation.     

Improved Properties of Bacillus coagulans β‐Galactosidase through Immobilization

Thermostable β‐galactosidase from Bacillus coagulans RCS3 was purified by successive column chromatography using DEAE‐cellulose and Sephadex G‐50. Immobilization of the purified enzyme was studied with DEAE‐cellulose and calcium alginate. The efficiency of β‐galactosidase retention was 87 % with DEAE‐cellulose (17 mg protein/mL of matrix) and 80 % with calcium alginate (2.2 mg protein/g bead). Comparative studies of immobilization displayed a shift in the optimum temperature from 65 °C to 70 °C provoked by DEAE‐cellulose, although no effect was observed with calcium alginate. The heat inactivation curve revealed an improvement in the stability (t_1/2 of 14.5 h for the immobilized enzyme as compared to 2 h for the free enzyme at 65 °C) in a calcium alginate system. This immobilized enzyme has a wide pH stability range (6.5–11). β‐Galactosidase immobilized by DEAE‐cellulose and calcium alginate allowed a 57 and 70 % lactose hydrolysis, respectively, to be achieved within 48 h after repeated use for twenty times.     

Solvent selection and optimization of α‐chymotrypsin‐catalyzed synthesis of N‐Ac‐Phe‐Tyr‐NH2 using mixture design and response surface methodology

A peptide, N‐Ac‐Phe‐Tyr‐NH₂, with angiotensin I‐converting enzyme (ACE) inhibitor activity was synthesized by an α‐chymotrypsin‐catalyzed condensation reaction of N‐acetyl phenylalanine ethyl ester (N‐Ac‐Phe‐OEt) and tyrosinamide (Tyr‐NH₂). Three kinds of solvents: a Tris–HCl buffer (80 mM, pH 9.0), dimethylsulfoxide (DMSO), and acetonitrile were employed in this study. The optimum reaction solvent component was determined by simplex centroid mixture design. The synthesis efficiency was enhanced in an organic‐aqueous solvent (Tris‐HCl buffer: DMSO: acetonitrile = 2:1:1) in which 73.55% of the yield of N‐Ac‐Phe‐Tyr‐NH₂ could be achieved. Furthermore, the effect of reaction parameters on the yield was evaluated by response surface methodology (RSM) using a central composite rotatable design (CCRD). Based on a ridge max analysis, the optimum condition for this peptide synthesis included a reaction time of 7.4 min, a reaction temperature of 28.1°C, an enzyme activity of 98.9 U, and a substrate molar ratio (Phe:Tyr) of 1:2.8. The predicted and the actual (experimental) yields were 87.6 and 85.5%, respectively. The experimental design and RSM performed well in the optimization of synthesis of N‐Ac‐Phe‐Tyr‐NH₂, so it is expected to be an effective method for obtaining a good yield of enzymatic peptide. © 2012 American Institute of Chemical Engineers Biotechnol. Prog., 2012     

Enantioselective synthesis of (S)‐naproxen using immobilized lipase on chitosan beads

S‐naproxen by enantioselective hydrolysis of racemic naproxen methyl ester was produced using immobilized lipase. The lipase enzyme was immobilized on chitosan beads, activated chitosan beads by glutaraldehyde, and Amberlite XAD7. In order to find an appropriate support for the hydrolysis reaction of racemic naproxen methyl ester, the conversion and enantioselectivity for all carriers were compared. In addition, effects of the volumetric ratio of two phases in different organic solvents, addition of cosolvent and surfactant, optimum pH and temperature, reusability, and inhibitory effect of methanol were investigated. The optimum volumetric ratio of two phases was defined as 3:2 of aqueous phase to organic phase. Various water miscible and water immiscible solvents were examined. Finally, isooctane was chosen as an organic solvent, while 2‐ethoxyethanol was added as a cosolvent in the organic phase of the reaction mixture. The optimum reaction conditions were determined to be 35 °C, pH 7, and 24 h. Addition of Tween‐80 in the organic phase increased the accessibility of immobilized enzyme to the reactant. The optimum organic phase compositions using a volumetric ratio of 2‐ethoxyethanol, isooctane and Tween‐80 were 3:7 and 0.1% (v /v/v), respectively. The best conversion and enantioselectivity of immobilized enzyme using chitosan beads activated by glutaraldehyde were 0.45 and 185, respectively.     

Fed‐batch synthesis of galacto‐oligosaccharides with Aspergillus oryzae β‐galactosidase using optimal control strategy

Fed‐batch synthesis of galacto‐oligosaccharides (GOS) from lactose with β‐galactosidase from Aspergillus oryzae was evaluated experimentally and reaction yield was maximized via optimal control technique. The optimal lactose and enzyme feed flow rate profiles were determined using a model for GOS synthesis previously reported by the authors. Experimentally it was found that fed‐batch synthesis allowed an increase on the maximum total GOS concentration from 115 (batch synthesis) to 218 g L^?1 as consequence of the increase in total sugars concentration from 40 to 58% w/w. Such high concentration of total sugars was not attainable in batch operation because of the low solubility of lactose at the reaction temperature (40°C). Simulations predicted a GOS yield of 32.5 g g^?1 in fed‐batch synthesis under optimal conditions, while experimentally the same yield as in batch synthesis was obtained (28 g g^?1). Besides, an enrichment of total oligosaccharides in GOS with a high polymerization degree (GOS‐5 and GOS‐6) was observed in the fed‐batch synthesis. Experimental profiles for all sugars were similar to the ones predicted by simulation, which supports the use of this methodology for the optimization of GOS synthesis. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 30:59–67, 2014     

In situ immobilization of β‐galactosidase from Bacillus circulans in silica by sol‐gel process: Application in prebiotic synthesis

The enzyme encapsulation is a very well‐known stabilization pathway. However, there are some challenges in order to avoid the enzyme denaturation under encapsulation conditions. The β‐galactosidase from Bacillus circulans was immobilized through sol‐gel encapsulation route assisted by Triton X‐100 surfactant and sugars. The effects of sugar presence in the immobilization process and the gelation time on the biocatalyst activity/stability were explained taking into account the characteristics of the formed silica matrix and the changes of the enzyme environment. The enzyme was effectively immobilized by this strategy, with high immobilization yield in terms of activity (29%) and expressed activity (47 IU/g). The immobilization through silica sol‐gel in the presence of 1×10^?3 M Triton X‐100 and fructose conferred 28.4‐fold higher stability to the enzyme compared with the soluble form. This is an advantage for its use in the synthesis of the galacto‐oligosaccharides at 50ºC. The total lactose conversion to galacto‐oligosaccharides was 26%wt, which is comparable with that reported in the literature. The obtained biocatalyst is useful for the synthesis of galacto‐oligosaccharides and its catalytic behavior is rationalized in this work.     

A pseudo steady‐state model for galacto‐oligosaccharides synthesis with β‐galactosidase from Aspergillus oryzae

A pseudo steady‐state model for the kinetically controlled synthesis of galacto‐oligosaccharides (GOS) with Aspergillus oryzae β‐galactosidase is presented. The model accounts for the dynamics of lactose consumption and production of galactose, glucose, di, tri, tetra, and penta‐oligosaccharides during the synthesis, being able to describe the total GOS content in the reaction medium at the experimental conditions evaluated. Experimental results show that the formation of GOS containing only galactose residues is significant at high conversions of substrate, which was taken into account in the model. The formation of enzyme transition complexes was considered and reasonable assumptions were made to reduce the number of parameters to be determined. The model developed has 8 parameters; 2 of them were experimentally determined and the other 6 were estimated by fitting to the experimental data using multiresponse regression. Temperature effect on kinetic and affinity constants was determined in the range from 40 to 55°C, and the data were fitted to Arrhenius type equation. Parameters of the proposed model are independent from the enzyme load in the reaction medium and, differently from previously reported models, they have a clear biochemical meaning. The magnitude of the kinetic and affinity constants of the enzyme suggests that the liberation of galactose from the galactosyl–enzyme complex is a very slow reaction and such complex is driven into GOS formation. It also suggests that the affinity for sugars of the galactosyl–enzyme complex is higher than that of the free enzyme. Biotechnol. Bioeng. 2011;108: 2270–2279. © 2011 Wiley Periodicals, Inc.     

Design of β‐galactosidase/silica biocatalysts: Impact of the enzyme properties and immobilization pathways on their catalytic performance

The use of heterogeneous biocatalysis in industrial applications is advantageous and the enzyme stability improvement is a continuous challenge. Therefore, we designed β‐galactosidase heterogeneous biocatalysts by immobilization, involving the support synthesis and enzyme selection (from Bacillus circulans, Kluyveromyces lactis, and Aspergillus oryzae). The underivatized, tailored, macro‐mesoporous silica exhibited high surface area, offered high enzyme immobilization yields and activity. Its chemical activation with glyoxyl groups bound the enzyme covalently, which suppressed lixiviation and conferred higher pH and thermal stability (120‐fold than for the soluble enzyme), without observable reduction of activity/stability due to the presence of silica. The best balance between the immobilization yield (68%), activity (48%), and stability was achieved for Bacillus circulans β‐galactosidase immobilized on glyoxyl‐activated silica, without using stabilizing agents or modifying the enzyme. The enzyme stabilization after immobilization in glyoxyl‐activated silica was similar to that observed in macroporous agarose‐glyoxyl support, with the reported microbiological and mechanical advantages of inorganic supports. The whey lactolysis at pH 6.0 and 25°C by using this catalyst (1 mg ml^?1, 290 UI g^?1) was still 90%, even after 10 cycles of 10 min, in batch process but it could be also implemented on continuous processes at industrial level with similar results.     

Bioreaction Engineering Leading to Efficient Synthesis of L‐Glyceraldehyd‐3‐Phosphate

Enantiopure L‐glyceraldehyde‐3‐phosphate (L‐GAP) is a useful building block in natural biological and synthetic processes. A biocatalytic process using glycerol kinase from Cellulomonas sp. (EC 2.7.1.30) catalyzed phosphorylation of L‐glyceraldehyde (L‐GA) by ATP is used for the synthesis of L‐GAP. L‐GAP has a half‐life of 6.86 h under reaction conditions. The activity of this enzyme depends on the Mg²⁺ to ATP molar ratio showing maximum activity at the optimum molar ratio of 0.7. A kinetic model is developed and validated showing a 2D correlation of 99.9% between experimental and numerical data matrices. The enzyme exhibits inhibition by ADP, AMP, methylglyoxal and Ca²⁺, but not by L‐GAP and inorganic orthophosphate. Moreover, equal amount of Ca²⁺ exerts a different degree of inhibition relative to the activity without the addition of Ca²⁺ depending on the Mg²⁺ to ATP molar ratio. If the Mg²⁺ to ATP molar ratio is set to be at the optimum value or less, inorganic hexametaphosphate (PPi6) suppresses the enzyme activity; otherwise PPi6 enhances the enzyme activity. Based on reaction engineering parameters such as conversion, selectivity and specific productivity, evaluation of different reactor types reveals that batchwise operation via stirred‐tank reactor is the most efficient process for the synthesis of L‐GAP.     

A novel enzymatic microreactor with Aspergillus oryzae β‐galactosidase immobilized on silicon dioxide nanosprings

The use of silicon dioxide (SiO₂) nanosprings as supports for immobilized enzymes in a continuous microreactor is described. A nanospring mat (2.2 cm² × 60 μm thick) was functionalized with γ‐aminopropyltriethoxysilane, then treated with N‐succinimidyl‐3‐(2‐pyridyldithio)‐propionate (SPDP) and dithiothreitol (DTT) to produce surface thiol (? SH) groups. SPDP‐modified β‐galactosidase from Aspergillus oryzae was immobilized on the thiolated nanosprings by reversible disulfide linkages. The enzyme‐coated nanospring mat was placed into a 175‐μm high microchannel, with the mat partially occluding the channel. The kinetics and steady‐state conversion of hydrolysis of o‐nitrophenyl β‐D ‐galactosylpyranoside at various substrate flow rates and concentrations were measured. Substantial flow was observed through the nanosprings, for which the Darcy permeability κ ≈ 3 × 10^?6 cm². A simple, one‐parameter numerical model coupling Navier‐Stokes and Darcy flow with a pseudo‐first‐order reaction was used to fit the experimental data. Simulated reactor performance was sensitive to changes in κ and the height of the nanospring mat. Permeabilities lower than 10^?8 cm² practically eliminated convective flow through the nanosprings, and substantially decreased conversion. Increasing the height of the mat increased conversion in simulations, but requires more enzymes and could cause sealing issues if grown above channel walls. Preliminary results indicate that in situ regeneration by reduction with DTT and incubation with SPDP‐modified β‐galactosidase is possible. Nanosprings provide high solvent‐accessible surface area with good permeability and mechanical stability, can be patterned into existing microdevices, and are amenable to immobilization of biomolecules. Nanosprings offer a novel and useful support for enzymatic microreactors, biosensors, and lab‐on‐chip devices. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Stability and kinetic behavior of immobilized laccase from Myceliophthora thermophila in the presence of the ionic liquid 1‐ethyl‐3‐methylimidazolium ethylsulfate

The use of ionic liquids (ILs) as reaction media for enzymatic reactions has increased their potential because they can improve enzyme activity and stability. Kinetic and stability properties of immobilized commercial laccase from Myceliophthora thermophila in the water‐soluble IL 1‐ethyl‐3‐methylimidazolium ethylsulfate ([emim][EtSO₄]) have been studied and compared with free laccase. Laccase immobilization was carried out by covalent binding on glyoxyl–agarose beads. The immobilization yield was 100%, and the activity was totally recovered. The Michaelis‐Menten model fitted well to the kinetic data of enzymatic oxidation of a model substrate in the presence of the IL [emim][EtSO₄]. When concentration of the IL was augmented, the values of V_max for free and immobilized laccases showed an increase and slight decrease, respectively. The laccase–glyoxyl–agarose derivative improved the laccase stability in comparison with the free laccase regarding the enzymatic inactivation in [emim][EtSO₄]. The stability of both free and immobilized laccase was slightly affected by small amounts of IL (<50%). A high concentration of the IL (75%) produced a large inactivation of free laccase. However, immobilization prevented deactivation beyond 50%. Free and immobilized laccase showed a first‐order thermal inactivation profile between 55 and 70°C in the presence of the IL [emim][EtSO₄]. Finally, thermal stability was scarcely affected by the presence of the IL. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:790–796, 2014     

Peptide backbone cleavage by α‐amidation is enhanced at methionine residues

Cleavage reactions at backbone loci are one of the consequences of oxidation of proteins and peptides. During α‐amidation, the C_α–N bond in the backbone is cleaved under formation of an N‐terminal peptide amide and a C‐terminal keto acyl peptide. On the basis of earlier works, a facilitation of α‐amidation by the thioether group of adjacent methionine side chains was proposed. This reaction was characterized by using benzoyl methionine and benzoyl alanyl methionine as peptide models. The decomposition of benzoylated amino acids (benzoyl‐methionine, benzoyl‐alanine, and benzoyl‐methionine sulfoxide) to benzamide in the presence of different carbohydrate compounds (reducing sugars, Amadori products, and reductones) was studied during incubation for up to 48 h at 80 °C in acetate‐buffered solution (pH 6.0). Small amounts of benzamide (0.3–1.5 mol%) were formed in the presence of all sugars and from all benzoylated species. However, benzamide formation was strongly enhanced, when benzoyl methionine was incubated in the presence of reductones and Amadori compounds (3.5–4.2 mol%). The reaction was found to be intramolecular, because α‐amidation of a similar 4‐methylbenzoylated amino acid was not enhanced in the presence of benzoyl‐methionine and carbohydrate compounds. In the peptide benzoyl‐alanyl‐methionine, α‐amidation at the methionine residue is preferred over α‐amidation at the benzoyl peptide bond. We propose here a mechanism for the enhancement of α‐amidation at methionine residues. Copyright © 2014 European Peptide Society and John Wiley & Sons, Ltd.     

Enzymatic Synthesis of Carbohydrate Derivatives Using β-Glycosidase of Sulfolobus Solfataricus

Enzymatic synthesis of different β-D-glycosides was obtained using as biocatalyst immobilized cells, crude homogenate, and homogeneous native and recombinat β-glycosidase activity of the thermophilic archaeon Sulfolobus solfataricus. In particular our investigation was concerned with the selectivity in the glycosylation of hydroxybenzyl alcohols, salicin, 1,2-propanediol, and more complex polyols as well as the use of immobilized cells for the synthesis of hexyl-β-D-glucoside. The aromatic glucosides obtained by enzyme-catalyzed transglucosylation were used for kinetic studies of purified Sulfolobus solfataricus enzyme in the hydrolysis reaction.     

Simultaneous synthesis of 2‐phenylethanol and L‐homophenylalanine using aromatic transaminase with yeast Ehrlich pathway

2‐Phenylethanol is a widely used aroma compound with rose‐like fragrance and L ‐homophenylalanine is a building block of angiotensin‐converting enzyme (ACE) inhibitor. 2‐phenylethanol and L ‐homophenylalanine were synthesized simultaneously with high yield from 2‐oxo‐4‐phenylbutyric acid and L ‐phenylalanine, respectively. A recombinant Escherichia coli harboring a coupled reaction pathway comprising of aromatic transaminase, phenylpyruvate decarboxylase, carbonyl reductase, and glucose dehydrogenase (GDH) was constructed. In the coupled reaction pathway, the transaminase reaction was coupled with the Ehrlich pathway of yeast; (1) a phenylpyruvate decarboxylase (YDR380W) as the enzyme to generate the substrate for the carbonyl reductase from phenylpyruvate (i.e., byproduct of the transaminase reaction) and to shift the reaction equilibrium of the transaminase reaction, and (2) a carbonyl reductase (YGL157W) to produce the 2‐phenylethanol. Selecting the right carbonyl reductase showing the highest activity on phenylacetaldehyde with narrow substrate specificity was the key to success of the constructing the coupling reaction. In addition, NADPH regeneration was achieved by incorporating the GDH from Bacillus subtilis in the coupled reaction pathway. Based on 40 mM of L ‐phenylalanine used, about 96% final product conversion yield of 2‐phenylethanol was achieved using the recombinant E. coli. Biotechnol. Bioeng. 2009;102: 1323–1329. © 2008 Wiley Periodicals, Inc.     

Heterofunctional Magnetic Metal‐Chelate‐Epoxy Supports for the Purification and Covalent Immobilization of Benzoylformate Decarboxylase From Pseudomonas Putida and Its Carboligation Reactivity

In this study, the combined use of the selectivity of metal chelate affinity chromatography with the capacity of epoxy supports to immobilize poly‐His‐tagged recombinant benzoylformate decarboxylase from Pseudomonas putida (BFD, E.C. 4.1.1.7) via covalent attachment is shown. This was achieved by designing tailor‐made magnetic chelate–epoxy supports. In order to selectively adsorb and then covalently immobilize the poly‐His‐tagged BFD, the epoxy groups (300 µmol epoxy groups/g support) and a very small density of Co²⁺‐chelate groups (38 µmol Co²⁺/g support) was introduced onto magnetic supports. That is, it was possible to accomplish, in a simple manner, the purification and covalent immobilization of a histidine‐tagged recombinant BFD. The magnetically responsive biocatalyst was tested to catalyze the carboligation reactions. The benzoin condensation reactions were performed with this simple and convenient heterogeneous biocatalyst and were comparable to that of a free‐enzyme‐catalyzed reaction. The enantiomeric excess (ee) of (R)‐benzoin was obtained at 99 ± 2% for the free enzyme and 96 ± 3% for the immobilized enzyme. To test the stability of the covalently immobilized enzyme, the immobilized enzyme was reused in five reaction cycles for the formation of chiral 2‐hydroxypropiophenone (2‐HPP) from benzaldehyde and acetaldehyde, and it retained 96% of its original activity after five reaction cycles. Chirality 27:635–642, 2015. © 2015 Wiley Periodicals, Inc.     

Application of Exchangeable Biochemical Reactors with Oxidase‐Catalase‐Co‐immobilizates and Immobilized Microorganisms in a Microfluidic Chip‐Calorimeter

Several methods for the quantitative detection of different compounds, e.g., L‐amino acids, sugars or alcohols in liquid media were developed by application of an automatic measuring unit including a fluid chip‐calorimeter FCC‐21. For this purpose, enzymes were immobilized covalently on the inner and outer surface of CPG (controlled porous glass)‐spherules with an outer diameter of 100 μm and filled into a micro flow‐through reaction chamber (V_R = 20 μL). The design of the measuring cell allows for easy insertion into the calorimeter device of a stored series of comfortably pre‐fabricated measuring cells. These cells can be filled with different enzyme immobilizates. Different oxidases were used and co‐immobilized with catalase for the improvement of the detection sensitivity. A signal amplification could be achieved up to a factor of 3.5 with this configuration. β‐D‐glucose, ethanol and L‐lysine could be detected in a range of 0.25–1.75 mM using glucose oxidase, alcohol oxidase and lysine oxidase. The group of oxidases in combination with the enzymatic catalysis of the intermediate H₂O₂ allows the quantitative detection of a large number of analytes. A good measurement and storage stability could be achieved for several weeks by this immobilization method. In addition to enzyme‐based detection reactions, it was shown that living microorganisms can be immobilized in the reaction chamber. Thus, the system can be used as a whole‐cell biosensor. The quantitative detection of phenol in the range of 10–100 μM could be performed using the actinomycete Rhodococcus sp. immobilized on glass beads by means of embedding into polymers.     

Highly efficient enzymatic synthesis of an ascorbyl unstaturated fatty acid ester with ecofriendly biomass‐derived 2‐methyltetrahydrofuran as cosolvent

Enzymatic synthesis of ascorbyl undecylenate, an unsaturated fatty acid ester of ascorbic acid, was reported with biomass‐derived 2‐methyltetrahydrofuran (MeTHF) as the cosolvent. Of the immobilized lipases tested, Candida antarctica lipase B (CAL‐B) showed the highest activity for enzymatic synthesis of ascorbyl undecylenate. Effect of reaction media on the enzymatic reaction was studied. The cosolvent mixture, t‐butanol‐MeTHF (1:4, v/v) proved to be the optimal medium, in which not only ascorbic acid had moderate solubility, but also CAL‐B showed a high activity, thus addressing the major problem of the solvent conflict for dissolving substrate and keeping satisfactory enzyme activity. In addition, the enzyme was much more stable in MeTHF and t‐butanol‐MeTHF (1:4) than in previously widely used organic solvents, t‐butanol, 2‐methyl‐2‐butanol, and acetone. The much higher initial reaction rate in this cosolvent mixture may be rationalized by the much lower apparent activation energy of this enzymatic reaction (26.6 vs. 38.1–39.1 kJ/mol) and higher enzyme catalytic efficiency (V_max/K_m, 8.4 vs. 1.3–1.4 h^?1). Ascorbyl undecylenate was obtained with the yields of 84–89% and 6‐regioselectivity of >99% in t‐butanol‐MeTHF (1:4) at supersaturated substrate concentrations (60 and 100 mM) after 5–8 h. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1005–1011, 2014     

Enzymatic synthesis of β‐glucosylglycerol using a continuous‐flow microreactor containing thermostable β‐glycoside hydrolase CelB immobilized on coated microchannel walls

β‐Glucosylglycerol (βGG) has potential applications as a moisturizing agent in cosmetic products. A stereochemically selective method of its synthesis is kinetically controlled enzymatic transglucosylation from a suitable donor substrate to glycerol as acceptor. Here, the thermostable β‐glycosidase CelB from Pyrococcus furiosus was used to develop a microstructured immobilized enzyme reactor for production of βGG under conditions of continuous flow at 70°C. Using CelB covalently attached onto coated microchannel walls to give an effective enzyme activity of 30 U per total reactor working volume of 25 µL, substrate conversion and formation of transglucosylation product was monitored in dependence of glucosyl donor (2‐nitrophenyl‐β‐D ‐glucoside (oNPGlc), 3.0 or 15 mM; cellobiose, 250 mM), the concentration of glycerol (0.25–1.0 M), and the average residence time (0.2–90 s). Glycerol caused a concentration‐dependent decrease in the conversion of the glucosyl donor via hydrolysis and strongly suppressed participation of the substrate in the reaction as glucosyl acceptor. The yields of βGG were ≥80% and ≈60% based on oNPGlc and cellobiose converted, respectively, and maintained up to near exhaustion of substrate (≥80%), giving about 120 mM (30 g/L) of βGG from the reaction of cellobiose and 1 M glycerol. The structure of the transglucosylation products, 1‐O‐β‐D ‐glucopyranosyl‐rac‐glycerol (79%) and 2‐O‐β‐D ‐glucopyranosyl‐sn‐glycerol (21%), was derived from NMR analysis of the product mixture of cellobiose conversion. The microstructured reactor showed conversion characteristics similar to those for a batchwise operated stirred reactor employing soluble CelB. The advantage of miniaturization to the microfluidic format lies in the fast characterization of full reaction time courses for a range of process conditions using only a minimum amount of enzyme. Biotechnol. Bioeng. 2009;103: 865–872. © 2009 Wiley Periodicals, Inc.     

Synthesis of dipeptide precursors with an immobilized thermolysin in ethyl acetate

N-(Benzyloxycarbonyl)-L-aspartyl-L-phenylalanine methyl ester (Z-AspPheOMe), a precursor of the aspartame, and N-(benzyloxycarbonyl)-L-phenylalanyl-Lphenylalanine methyl ester (Z-PhePheOMe) were synthesized from the respective amino acid derivatives with an immobilized thermolysin (EC 3.4.24.4) in ethyl acetate. Various factors affecting the synthesis of these dipeptide precursors were clarified. The initial synthetic rate was the highest at the water content of 3.5% for both reactions. The substrate concentration dependencies of the initial synthetic rate of Z-AspkPheOMe and Z-PhePheOMe with the immobilized enzyme in ethyl acetate were different from those in an aqueous buffer solution saturated with ethyl acetate but similar to those in the aqueous/organic biphasic system using the free enzyme. Particularly, the initial synthetic rate of Z-AspPhOMe increased in order higher than first order with respect to the concentration of L-phenylalanine methyl ester (PheOMe), whereas it decreased sharply with the concentration of N-(benzyloxycarbonyl)-L-aspartic acid (Z-Asp). Such kinetic behavior could be explained by regarding the inside of the immobilized enzyme as being a biphasic mode composed from the organic phase and aqueous phase where the enzymatic reaction takes place. The reaction in the aqueous/organic biphasic system using the free enzyme could be simulated by taking into consideration the partition of the substrate and the initial rate of synthesis in the aqueous buffer saturated with ethyl acetate. Based on this analysis, the rate of reaction with the immobilized enzyme in ethyl acetate could also be predicted. Z-AsPheOMe and Z-PhePheOMe were synthesized by the fed-batch method where the acid component of the substrate was intermittently added during the course of reaction and by the batch method. In the synthesis of Z-AspPheOMe, the synthetic rate and maximum yield of reaction as well as the stability of the immobilized enzyme were higher in the fed-batch reaction than those in the batch reaction. In the synthesis of Z-PhePheOMe, the results obtained by both methods were similar. (c) 1994 John Wiley & Sons, Inc.