Kinetic modeling of omega-transamination for enzymatic kinetic resolution of alpha-methylbenzylamine

A kinetic model for omega-transaminase from Bacillus thuringiensis JS64 was developed by using the King-Altman method to simulate the kinetic resolution of alpha-methylbenzylamine (alpha-MBA). Starting from a ping-pong bi-bi mechanism, a complete kinetic model including substrate inhibition only in the reverse reaction (i.e., transamination between acetophenone and L-alanine) was developed. The asymmetric synthesis of (S)-alpha-MBA proved to be difficult due to a much lower maximum reverse reaction rate than the maximum forward reaction rate, thermodynamically exergonic forward reaction (i.e., transamination between (S)-alpha-MBA and pyruvate), and the severe product and substrate inhibition of the reverse reaction. Experimental values for kinetic parameters show that the product inhibition constant of (S)-alpha-MBA is the most important parameter on determining the resolution reaction rate, suggesting that the resolution reaction rate will be very low unless (S)-alpha-MBA strongly inhibits the reverse reaction. Using the kinetic model, the kinetic resolution of alpha-MBA in aqueous buffer was simulated, and the simulation results showed a high degree of consistency with experimental data over a range of reaction conditions. Various simulation results suggest that the crucial bottleneck in the kinetic resolution of alpha-MBA lies mainly in the accumulation of acetophenone in reaction media as the reaction proceeds, whereas L-alanine exerts a little inhibitory effect on the reaction. The model predicts that removing acetophenone produced during the reaction can enhance the reaction rate dramatically. Indeed, the biphasic reaction system is capable of extracting acetophenone from the aqueous phase, showing a much higher reaction rate compared to a monophasic reaction system. The kinetic model was also useful in predicting the properties of other, better enzymes as well as the optimal concentrations of amino acceptor and enzyme in the resolution reaction.     

Microbial synthesis of ethyl (R)-4,4,4-trifluoro-3-hydroxybutanoate by asymmetric reduction of ethyl 4,4,4-trifluoroacetoacetate in an aqueous-organic solvent biphasic system

In this study, whole cells of Saccharomyces uvarum SW-58 were applied in an aqueous-organic solvent biphasic system for the asymmetric reduction of ethyl 4,4,4-trifluoroacetoacetate to ethyl (R)-4,4,4-trifluoro-3-hydroxybutanoate [(R)-2]. The results of reduction in different aqueous-organic solvent biphasic systems showed that dibutylphthalate provided the best compromise between the biocompatibility and the partition of substrate and product among the solvents tested. To optimize the reaction, several factors such as reaction pH, temperature, shaking speed, volume ratio of the aqueous phase to the organic phase and ratio of biomass/substrate were investigated. It was found that the change of these factors obviously influenced the conversion and initial reaction rate, and had a minor effect on the enatiomeric excess of the product. Under the optimal conditions, 85.0% of conversion and 85.2% of enatiomeric excess were achieved. The bioconversion in the biphasic system was more efficient compared with that in the monophasic aqueous system, and product concentration as high as 54.6 g/L was reached in the organic phase without addition of co-enzyme.     

Kinetics of enzymatic synthesis of peptides in aqueous/organic biphasic systems. Thermolysin-catalyzed synthesis of N-(benzyloxycarbonyl)-L-phenylalanyl-L-phenylalanine methyl ester

We studied kinetics of thermolysin-catalyzed peptide synthesis in an aqueous/organic biphasic system theoretically and experimentally. As a model reaction producing a condensation product having no dissociating groups, we used the synthesis of N-(benzyloxycarbonyl)-L-phenylalanyl-L-phenylalanine methyl ester (Z-Phe2OMe) from N-(benzyloxycarbonyl)-L-phenylalanine (Z-Phe) and L-phenylalanine methyl ester (PheOMe). Usually, ethyl acetate was used as the organic solvent. First we studied the kinetics of the synthesis of Z-Phe2OMe in a buffer solution saturated with ethyl acetate. Then, factors that may affect the kinetics in the biphasic system were examined. The course of Z-Phe2OMe synthesis in the biphasic system was explained by the rate equations obtained, using the partitions of substrate and product and non-enzymatic decomposition of PheOMe. In the biphasic reaction system, the rate of synthesis was lower for a wide range of pH due to the unfavorable partition of PheOMe in the aqueous phase, but yields were higher than in the buffer solution. The effects of the organic solvents on the rate of synthesis could also be explained by variations in the partition coefficient of PheOMe. Finally, we gave a way to predict the aqueous-phase pH change caused by partitioning of the substrate. The significance of the pH change was shown in connection with the reaction using the immobilized enzyme in an organic solvent.     

Enzymatic synthesis of the precursor of Leu-enkephalin in water-immiscible organic solvent systems.

The precursor of Leu-enkephalin, Z-L-TyrGlyGly-L-Phe-L-LeuOEt, was synthesized from amino acid derivatives with three proteinases without the protection of the side chain of L-Tyr. First, Z-GlyGlyOBut and Z-L-TyrGlyGlyOBut were synthesized in quite a high yield, 83% and 99%, in an aqueous/organic biphasic system by papain and alpha-chymotrypsin, respectively. Then, Z-L-Phe-L-LeuOEt was synthesized by thermolysin from Z-L-Phe and L-LeuOEt either in buffer or in a biphasic system; the yields were 95% and 100%, respectively. The synthesis of Z-L-TyrGlyGly-L-Phe-L-LeuOEt from Z-L-TyrGlyGly and L-Phe-L-LeuOEt was performed effectively by thermolysin immobilized on Amberlite XAD-7 in a buffer and in an aqueous/organic biphasic system, as well as in saturated ethyl acetate, while the yield was low in reactions by free thermolysin. In the reaction with the immobilized enzyme (IME) in saturated ethyl acetate, the maximum yield of the precursor of Leu-enkephalin was 68%. The reasons for effective synthesis with IME are: (1) higher concentration of L-Phe-L-LeuOEt inside support, which resulted in rising the rate of the synthesis reaction and protecting the competitive hydrolysis of Z-L-TyrGlyGly by thermolysin, (2) entrapment of the product inside the support where thermolysin could not act in the case of reaction in buffer, and (3) extraction of the product with the organic solvent in the case of reaction in a biphasic system or in saturated organic solvent.     

Repeated batch and continuous syntheses of N-(benzyloxycarbonyl)-l-phenylalanyl-l-phenylalanine methyl ester with immobilized thermolysin

Summary N-(Benzyloxycarbonyl)-l-phenylalanyl-l-phenylalanine methyl ester was synthesized from N-(benzyloxycarbonyl)-l-phenylalanine and l-phenylalanine methyl ester in an aqueous solution (aqueous phasic reaction), in an aqueous/organic biphasic system (biphasic reaction), and in an organic solvent (organic phasic reaction) with immobilized thermolysin. In the aqueous phasic reaction with thermolysin immobilized on Amberlite XAD-7, the whole product was trapped inside the support; extraction with ethyl acetate was needed to recover the product, and the equilibrium yield was low (about 65%). With the biphasic and organic phasic reactions with ethyl acetate as an organic solvent, the yield was around 95%. Because of the high yield and feasibility of operation, repeated batch and continuous reactions were done in the biphasic and organic phasic systems, respectively. The half-lives of the activity for the immobilized enzyme used in the biphasic system at 40°C by repeated batch operation and in a plug flow reactor fed with substrate dissolved in ethyl acetate at 40°C and 30°C were estimated to be about 200 h (67 batches), 420 h, and 1100 h, respectively.     

Kinetic resolution of chiral amines with omega-transaminase using an enzyme-membrane reactor

A kinetic resolution process for the production of chiral amines was developed using an enzyme-membrane reactor (EMR) and a hollow-fiber membrane contactor with (S)-specific omega-transaminases (omega-TA) from Vibrio fluvialis JS17 and Bacillus thuringiensis JS64. The substrate solution containing racemic amine and pyruvate was recirculated through the EMR and inhibitory ketone product was selectively extracted by the membrane contactor until enantiomeric excess of (R)-amine exceeded 95%. Using the reactor set-up with flat membrane reactor (10-mL working volume), kinetic resolutions of alpha-methylbenzylamine (alpha-MBA) and 1-aminotetralin (200 mM, 50 mL) were carried out. During the operation, concentration of ketone product, i.e., acetophenone or alpha-tetralone, in a substrate reservoir was maintained below 0.1 mM, suggesting efficient removal of the inhibitory ketone by the membrane contactor. After 47 and 32.5 h of operation using 5 U/mL of enzyme, 98.0 and 95.5% ee of (R)-alpha-MBA and (R)-1-aminotetralin were obtained at 49.5 and 48.8% of conversion, respectively. A hollow-fiber membrane reactor (39-mL working volume) was used for a preparative-scale kinetic resolution of 1-aminotetralin (200 mM, 1 L). After 133 h of operation, enantiomeric excess reached 95.6% and 14.3 g of (R)-1-aminotetralin was recovered (97.4% of yield). Mathematical modeling of the EMR process including the membrane contactor was performed to evaluate the effect of residence time. The simulation results suggest that residence time should be short to maintain the concentration of the ketone product in EMR sufficiently low so as to decrease conversion per cycle and, in turn, reduce the inhibition of the omega-TA activity.     

Kinetics and equilibrium of enzymatic synthesis of peptides in aqueous/organic biphasic systems. Thermolysin-catalyzed synthesis of N-(benzyloxycarbonyl)-L-aspartyl-L-phenylalanine methyl ester

We studied kinetics and the equilibrium relationship for the thermolysin-catalyzed synthesis of N-(benzyloxycarbonyl)-L-aspartyl-L-phenylalanine methyl ester (Z-Asp-PheOMe) from N-(benzyloxycarbonyl)-L-aspartic acid (Z-Asp) and L-phenylalanine methyl ester (PheOMe) in an aqueous-organic biphasic system. This is a model reaction giving a condensation product with dissociating groups. The kinetics for the synthesis of Z-Asp-PheOMe in aqueous solution saturated with ethyl acetate was expressed by a rate equation for the rapid-equilibrium random bireactant mechanism, and the reverse hydrolysis reaction was zero-order with respect to Z-Asp-PheOMe concentration. The courses of synthesis of Z-Asp-PheOMe in the biphasic system were well explained, by the rate equations obtained for the aqueous solution and by the partition of substrate and condensation product between the both phases. The rate of synthesis in the biphasic system was much lower than in aqueous solution due to the unfavorable partition of PheOMe in the aqueous phase. The equation for the equilibrium yield of Z-Asp-PheOMe in the biphasic system was derived assuming that only the non-ionized forms of the substrate and condensation product exist in the organic phase. It was found theoretically and experimentally that the yield of Z-Asp-PheOMe is maximum at the aqueous-phase pH of around 5, lower than for synthesis in aqueous solution. The effect of the organic solvent on the rate and equilibrium for the synthesis of Z-Asp-PheOMe could be explained by the variation in the partition coefficient. The effect of the partitioning of substrate on the aqueous-phase pH change was also shown.     

Interfacial versus homogeneous enzymatic cleavage of mandelonitrile by hydroxynitrile lyase in a biphasic system

The question of an interfacial versus a homogeneous reaction is carefully addressed for the enzymatic biphasic cleavage of mandelonitrile to benzaldehyde by Prunus amygdalus hydroxynitrile lyase (pa-Hnl) (Hickel et al. [1999] Biotechnol Bioeng 36:425-436). Experimental evidence, including 1) the reaction ceases when the interface is populated by previously adsorbed denatured pa-Hnl, 2) the reaction continues even after washout of the bulk enzyme from the aqueous phase, 3) highly nonpolar organic solvents initially promote fast reaction kinetics that relatively quickly decay to zero product production, and 4) the reaction rate is nonlinear in the bulk enzyme concentration, provide robust grounds for an interfacial reaction. We also model enzymatic mandelonitrile cleavage assuming a homogeneous aqueous-phase reaction. The homogeneous reaction scheme does not simultaneously account for the experimental observations of a linear dependence of the reaction rate on organic/water interfacial area, no dependence on the aqueous-phase volume, and a nonlinear dependence on pa-Hnl aqueous concentration. Further, simple calculations demonstrate that the homogeneous reaction rate is at least three orders of magnitude slower than those observed by Hickel et al. (1999). We again conclude that enzyme adsorbed at the organic solvent/water interface primarily catalyzes the biphasic mandelonitrile cleavage reaction.     

Comparison of the omega-transaminases from different microorganisms and application to production of chiral amines

Microorganisms that are capable of (S)-enantioselective transamination of chiral amines were isolated from soil samples by selective enrichment using (S)-alpha-methyl-benzylamine ((S)-alpha-MBA) as a sole nitrogen source. Among them, Klebsiella pneumoniae JS2F, Bacillus thuringiensis JS64, and Vibrio fluvialis JS17 showed good omega-transaminase (omega-TA) activities and the properties of the omega-TAs were investigated. The induction level of the enzyme was strongly dependent on the nitrogen source for the strains, except for V. fluvialis JS17. All the omega-TAs showed high enantioselectivity (E>50) toward (S)-alpha-MBA and broad amino donor specificities for arylic and aliphatic chiral amines. Besides pyruvate, aldehydes such as propionaldehyde and butyraldehyde showed good amino acceptor reactivities. All the omega-TAs showed substrate inhibition by (S)-alpha-MBA above 200 mm. Moreover, substrate inhibition by pyruvate above 10 mm was observed for omega-TA from V. fluvialis JS17. In the case of product inhibition, acetophenone showed much greater inhibitions than L-alanine for all omega-TAs. Comparison of the enzyme properties indicates that omega-transaminase from V. fluvialis JS17 is the best one for both kinetic resolution and asymmetric synthesis to produce enantiomerically pure chiral amines. Kinetic resolution of sec-butylamine (20 mM) was done under reduced pressure (150 Torr) to selectively remove an inhibitory product (2-butanone) using the enzyme from V. fluvialis JS17. Enantiomeric excess of (R)-sec-butylamine reached 94.7% after 12 h of reaction.     

Synthesis of (R)-2-trimethylsilyl-2-hydroxyl-propionitrile catalyzed by (R)-hydroxynitrile lyase from Prunus japonica seed meal

Synthesis of (R)-2-trimethylsilyl-2-hydroxyl-propionitrile via asymmetric transcyanation of acetyltrimethylsilane with acetone cyanohydrin in an aqueous/organic biphasic system catalyzed by (R)-hydroxynitrile lyase from Prunus japonica seed meal was successfully carried out for the first time. The optimal volume ratio of aqueous to organic phase, buffer pH value and reaction temperature were 15% (v/v), 5.0 and 30°C, respectively, under which both substrate conversion and product enantiomeric excess (ee) were 99%. Silicon atom in the substrate showed great effect on the reaction. Acetyltrimethylsilane was a much better substrate for (R)-hydroxynitrile lyase from Prunus japonica than its carbon analogue.     

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.     

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.     

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.     

Microbial oxidation of naphthalene to cis-1,2-naphthalene dihydrodiol using naphthalene dioxygenase in biphasic media

The selective oxidation of aryl substrates to chiral cis-1,2-dihydrodiols is an industrially important reaction for the production of intermediates that can be used to produce fine chemicals, pharmaceuticals, and many other bioactive natural products. More specifically, the oxidation of naphthalene to produce optically pure (+)-cis-(1R,2S)-1,2-napthalene dihydrodiol (NDHD) to be used as a chiral synthon for specialty chemicals has gained much interest. Escherichia coli JM109(DE3) pDTG141 expresses naphthalene dioxygenase which catalyzes this reaction. Poor substrate solubility and substrate toxicity are barriers to using the power of these enzymes in large-scale aqueous whole cell systems. A biphasic reaction system was chosen to overcome these barriers. The optimal biphasic conditions for E. coli JM109(DE3) pDTG141 were determined to be 20% dodecane as the organic solvent containing 40 g/L naphthalene. The productivity of the biotransformation using resting cells was 1.75 g-diol/g-cdw/h for the first 6 h with 20% organic phase, which was increased from 0.59 g-diol/g-cdw/h for growing cells with 40% organic phase. The biocatalytic activity was retained for at least 12 h. The biocatalyst could be recycled for at least four runs in both suspended and immobilized form. The stability of the 12 h recycle was improved by immobilization in calcium alginate beads. The process has been improved both environmentally and economically by reducing the amount of solvent used and by recycling the biocatalyst.     

Application of organic mono-phase and organic–aqueous two-liquid-phase systems in microalgal conversion of androst-4-en-3,17-dione by Nostoc muscorum

Organic mono-phase and organic–aqueous two-phase systems were applied for 17-carbonyl reduction of androst-4-en-3,17-dione to testosterone by whole cells of the microalga Nostoc muscorum (Nostocaceae). To investigate the correlation between solvent hydrophobicity and biotransformation yield in mono- and biphasic systems, a range of 16 organic solvents with log P_octanol values (logarithm of the solvent partition coefficient in the n-octanol/water system) between ? 1.1 and 8.8 were examined. Organic solvents with log P_octanol values greater than 7, such as hexadecane and tetradecane, provided the best biocompatibility with the bioconversion by algal cells. The data also indicated that the highest yields were obtained using organic–aqueous (1:1, v/v) biphasic systems. The optimum volumetric phase ratio, reaction temperature and substrate concentration were 1:1, 30°C and 0.5 mg mL^?1, respectively. Under the mentioned conditions a fourfold increase in biotransformation yield (from 7.8±2.3 to 33.4±1.8%) was observed.     

Model isolations of nucleic acids from prokaryotic and eukaryotic sources using an organic/aqueous biphasic system

Nucleic acids were extracted from bacteria and yeast, using a biphasic system created by mixing a water-miscible, organic solvent with an aqueous salt solution. Nucleic acids were separated from the majority of host-contaminating proteins without using chaotrophic agents such as guanidine salts, phenol or chloroform, which are known to be hazardous. Isolated DNA is sufficiently pure for use in the polymerase chain reaction (PCR).     

A new approach to preparative enzymatic synthesis. Reprinted from Biotechnology and Bioengineering, Vol. XIX, No. 9, Pages 1351-1361

A new approach to preparative organic synthesis in aqueous-organic systems is suggested. It is based on the idea that the enzymatic process is carried out in a biphasic system "water-water-immiscible organic solvent." Thereby the enzyme is localized in the aqueous phase-this eliminates the traditional problem of stabilizing the enzymes against inactivation by a nonaqueous solvent. Hence, in contrast to the commonly used combinations "water-water-miscible organic solvent," in the suggested system the content of water may be infinitely low. This allows one to dramatically shift the equilibrium of the reactions forming water as a reaction product (synthesis of esters and amides, polymerization of amino acids, sugars and nucleotides, dehydration reactions, etc.) toward the products. The fact that the system consists of two phases provides another very important sources for an equilibrium shift, i.e., free energies of the transfer of a reagent from one phase to the other. Equations are derived describing the dependence of the equilibrium constant in a biphasic system on the ratio of the volumes of the aqueous and nonaqueous phases and the partition coefficients of the reagents between the phases. The approach has been experimentally verified with the synthesis of N-acetyl-L-tryptophan ethyl ester from the respective alcohol and acid. Porous glass was impregnated with aqueous buffer solution of chymotrypsin and suspended in chloroform containing N-acetyl-L-tryptophan and ethanol. In water (no organic phase) the yield of the ester is about 0.01%, whereas in this biphasic system it is practically 100%. The idea is applicable to a great number of preparative enzymatic reactions.     

Synthesis of (R)-2-trimethylsilyl-2-hydroxyl-propionitrile catalyzed by (R)-hydroxynitrile lyase from Prunus japonica seed meal

Synthesis of (R)-2-trimethylsilyl-2-hydroxyl-propionitrile via asymmetric transcyanation of acetyltrimethylsilane with acetone cyanohydrin in an aqueous/organic biphasic system catalyzed by (R)-hydroxynitrile lyase from Prunus japonica seed meal was successfully carried out for the first time. The optimal volume ratio of aqueous to organic phase, buffer pH value and reaction temperature were 15% (v/v), 5.0 and 30°C, respectively, under which both substrate conversion and product enantiomeric excess (ee) were 99%. Silicon atom in the substrate showed great effect on the reaction. Acetyltrimethylsilane was a much better substrate for (R)-hydroxynitrile lyase from Prunus japonica than its carbon analogue.     

A new approach to preparative enzymatic synthesis

A new approach to preparative organic synthesis in aqueous–organic systems is suggested. It is based on the idea that the enzymatic process is carried out in a biphasic system “water–water-immiscible organic solvent.” Thereby the enzyme is localized in the aqueous phase—this eliminates the traditional problem of stabilizing the enzyme against inactivation by a nonaqueous solvent. Hence, in contrast to the commonly used combinations “water–water-miscible organic solvent,” in the suggested system the content of water may be infinitely low. This allows one to dramatically shift the equilibrium of the reactions forming water as a reaction product (synthesis of esters and amides, polymerization of amino acids, sugars and nucleotides, dehydration reactions, etc.) toward the products. The fact that the system consists of two phases provides another very important source for an equilibrium shift, i.e., free energies of the transfer of a reagent from one phase to the other. Equations are derived describing the dependence of the equilibrium constant in a biphasic system on the ratio of the volumes of the aqueous and nonaqueous phases and the partition coefficients of the reagents between the phases. The approach has been experimentally verified with the synthesis of N-acetyl-L -tryptophan ethyl ester from the respective alcohol and acid. Porous glass was impregnated with aqueous buffer solution of chymotrypsin and suspended in chloroform containing N-acetyl-L -tryptophan and ethanol. In water (no organic phase) the yield of the ester is about 0.01%, whereas in this biphasic system it is practically 100%. The idea is applicable to a great number of preparative enzymatic reactions.     

Enhancement of hydrolytic activity of sphingolipid ceramide N-deacylase in the aqueous-organic biphasic system

Lysoglycosphingolipids were produced from glycosphingolipids by using sphingolipid ceramide N-deacylase, which cleaves the N-acyl linkage between fatty acids and sphingosine bases in various glycosphingolipids. The enzyme reaction was done in a biphasic media prepared with water;-immiscible organic solvent and aqueous buffer solution containing the enzyme. We investigated the effects of organic solvents and detergents on lysoglycosphingolipid production in the biphasic system. Among the organic solvents tested, n-butylbenzene, cumene, cyclodecane, cyclohexane, n-decane, diisopropylether, n-heptadecane, and methylcyclohexane promoted hydrolysis of GM1, whereas benzene, chloroform, ethyl acetate, and toluene inhibited GM1 hydrolysis. Hydrolysis of asialo GM1, GD1a, GalCer, and sulfatide was also enhanced by the addition of n-decane. The hydrolytic activity of the enzyme was enhanced by the addition of 0.8% sodium taurodeoxycholate or sodium cholate to the aqueous phase. The most effective hydrolysis of various glycosphingolipids by the enzyme was thus obtained in the aqueous-n-decane biphasic system containing 0.8% sodium taurodeoxycholate. Under this condition, the fatty acids released from GM1 by the action of the enzyme were trapped and diffused into the organic phase, while lysoGM1 remained in the aqueous phase.Thus the almost complete hydrolysis of GM1 was achieved using the biphasic system, while at most 70% of hydrolysis was obtained using normal aqueous media possibly due to the inhibition of hydrolysis reaction by accumulation of fatty acids in the reaction mixture.