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.     

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.     

Synthesis of aspartame precursor with an immobilized thermolysin in mixed organic solvents

N-(benzyloxycarbonyl)-L-aspartyl-L-phenylalanine methyl ester, a precursor of the synthetic sweetener, aspartame, was synthesized from N-(benzyloxycarbonyl)-L-aspartic acid and L-phenylalanine methyl ester with an immobilized thermolysin (EC 3.4.24.4) in the mixed organic solvent system of tert-amyl alcohol and ethyl acetate. A mixed solvent consisting of tert-amyl alcohol and ethyl acetate at a ratio of 33:67 (v/v) was found to be the most suitable with respect to synthetic rate and stability of the immobilized enzyme. The reaction continued to proceed quite successfully in a column reactor at 40 degrees C and at a space velocity of 3.6 h(-1) with a yield of 99%, using 40 mM Z-Asp and 200 mM PheOMe dissolved in the mixed solvent as the substrate. (c) 1995 John Wiley & Sons, Inc.     

Hollow-Fibre Enzyme Reactor Integrated with Solvent Extraction for Synthesis of Aspartame Precursor

A new process for the simultaneous enzymic synthesis and purification of N-(benzyloxycarbonyl)- -aspartyl- -phenylalanine methyl ester (ZAPM), a precursor of aspartame, has been developed. The enzymic reaction between N-(benzyloxycarbonyl)- -aspartic acid (ZA) and -phenylalanine methyl ester (PM) was carried out in a biphasic hollow-fibre rector with an aqueous phase an a butyl acetate phase. The reaction took place in the aqueous phase and by maintaining the pH at 5, the product (ZAPM) was extracted into the organic phase. Product purity was greater than 90% and reasonable productivity could be achieved with this system.     

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.     

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.     

Kinetics of inhibition of thermolysin-catalyzed peptide synthesis by alcohols in aqueous organic one-phase system

The kinetic patterns and parameters of 12 alcoholic organic solvents of different classes inhibiting thermolysin-catalyzed synthesis of N-(benzyloxycarbonyl)-L-phenylalanyl-L-phenylalanine methyl ester (Z-Phe-Phe-OMe) in aqueous organic one-phase reaction system have been determined. All alcohols showed a linear mixed type inhibition. A kinetic model of inhibition is suggested. It was presumed that alcohols interact with substrate in the active site of thermolysin.     

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.     

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 aspartame precursor with an immobilized thermolysin in tert-amyl alcohol

N-(Benzyloxycarbonyl)-L-aspartyl-L-phenylalanine methyl ester (Z-AspPheOMe), a precursor of the synthetic sweetner asparatame, was synthesized from N-(benzyloxycarbolyl)-L-aspartic acid (Z-Asp) and L-phenylalanine methyl ester (PheOMe) with an immobilized thermolysin in various organic solvents. We found that in tert-amyl alcohol containing a small amount of water the immobilized enzyme showed a high activity comparble to that in ethyl acetate with quite a high stability. The immobilized enzyme was fully stable up to 70 degrees C in tert-amyl alcohol in the absence of the subatrate, and up to 50 degrees C in the presence of the substrate. The high stability in the presence of the substrate was found due to the fact that the release of calcium ions, the stabilizing factor of thermolysin, is suppressed.The substrate concentration dependence of the initial synthetic rate with the immobilized enzyme was quite different from that with the free enzyme in the biphasic system, in contrast to that in ethyl acetate. Finally, Z-AspPheOMe was continuously synthesized in a column reactor using 200 mM PheOMe and 120 mM Z-Asp as the substrate for over 300 h at 45 degrees C and a space velocity of 1 h(-1) without any loss of acivity. (c) 1994 John Wiley & Sons, Inc.     

Continuous production of N-(benzyloxycarbonyl)-L-glycyl-L-phenylalanine methyl ester utilizing extractive reaction in aqueous/organic biphasic medium

N-(Benzyloxycarbonyl)-L-glycyl-L-phenylalanine methyl ester was continuously synthesized, enzymatically, utilizing an extractive reaction in an aqueous/organic biphasic system. The extremely high yield, ca. 100%, was obtained continuously in a water/butyl acetate biphasic medium.     

Modification Effects of Organic Solvents on Microenvironment of the Enzyme in Thermolysin-catalyzed Peptide Synthesis of N-(Benzyloxycarbonyl)-l-phenylalanyl-l-phenylalanine Methyl Ester

Thermolysin-catalyzed peptide synthesis using N-benzyloxycarbonyl)-l-phenylalanine (Z-Phe) and l-phenylalanine methyl ester (Phe-OMe) as substrates was done mainly in a water-organic one phase solvent system. The organic solvent content used was less than the saturation concentration in buffer. With organic solvents with high log P values, the enzymatic activity increased as the organic solvent content increased; but further increases in the organic solvent content decreased the enzymatic activity, showing an “organic activity” profile. On the other hand, with organic solvents of low log P values, the enzymatic reaction was inhibited even by the initial addition of organic solvents. When a correlation between maximum activities and logP values or Hildebrand solubility parameters was investigated, a linear correlation was obtained among the same category of organic solvents, but not between categories. This suggests that the direct effect of organic solvents on the microenvironment of the enzyme largely depends on the molecular structure of the solvents.     

Synthesis of Aspartame Precursor Using Protease Suspended in Microaqueous Molten Amino Acids Mixture

Enzymatic synthesis of the aspartame precursor, N -(benzyloxycarbonyl)- l -aspartyl- l -phenylalanine methyl ester (Z-AspPheOMe) was performed with highly concentrated molten substrates. A mixture composed of molten N -(benzyloxycarbonyl)- l -aspartic acid (Z-Asp) and l -phenylalanine methyl ester (PheOMe) mixtures of 20 M could be prepared at 50°C. This Z-Asp/PheOMe mixture was applied to the enzymatic synthesis of Z-AspPheOMe using free thermolysin. Synthesis of Z-AspPheOMe was observed in the range of 100-150 &#119 l of NaOH solution (12.5 M) addition to a reaction mixture consisting of 1.0 mmol Z-Asp and 1.0 mmol PheOMe at 50°C. The enzymatic activity increased with increasing water addition, and reached a maximum at 100 &#119 l in addition to the reaction mixture of 1.0 mmol Z-Asp, 1.0 mmol PheOMe and 125 &#119 l of the NaOH solution. In this reaction system, the conversion at the reaction equilibrium was about 60%, the initial reaction rate calculated on the basis of the enzyme weight was 2.2 &#119 mol/g s, and the productivity calculated on the basis of the reaction mixture volume was 300 mol/m 3 h.     

Integration of charged membrane into perstraction system for separation of amino acid derivatives

The integration of a charged membrane into a perstraction system for high selective separation is reported. A mixture of N-(benzyloxycarbonyl)-L-aspartic acid (ZA), L-phenylalanine methyl ester (PM), and N-(benzyloxycarbonyl)-L-aspartyl-L-phenylalanine methyl ester (ZAPM) was used as the model solution. The aqueous phase containing ZA, PM, and ZAPM was adjusted to pH 6 and was contacted with tert-amyl alcohol through a charged membrane. Seven different ion-exchange membranes and two different microfiltration membranes were tested for the separation system. Only ZAPM could permeate into the organic phase through SELEMION AMV and ASV. The separations between ZA and ZAPM and between PM and ZAPM were performed by biphasic extraction and electrostatic rejection, respectively. The permeabilities of ZAPM were higher than those of PM for all experiments using the ion-exchange membranes, although the molecular weight of ZAPM is larger than that of PM. The membrane that had a smaller pore size showed higher ZAPM selectivity. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 162-167, 1997.     

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.     

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.     

Enzymes in preparative organic synthesis: Coincidence of the pH optimum for catalyst effectiveness with the pH optimum for the catalyzed reaction equilibrium

The study concerned the pH profile of the apparent equilibrium constant for synthesis of N-benzoyl-L -phenylalanine ethyl ester from the respective acid and ethanol in the biphasic system chloroform + 5% (v/v) water. The substitution of water (as a reaction medium) for the biphasic aqueous–organic system shifted the pH profile toward neutral pH values. As a result the pH range thermodynamically conducive to synthesis of the final product in the biphasic system coincided with the pH optimum of the catalytic activity of the enzyme used (α-chymotrypsin). This approach should, in principle, be considered as general: first, per se it is independent of a catalyst (enzyme) nature; second, the biphasic method helps the shift ionic equilibria involving not only organic acids, but also bases. A physical mechanism of the ionic equilibrium shift is the same is both cases, namely, a preferable extraction from water into an organic phase of one generally nonionic (more hydrophobic) form of the reagent.     

Enzymatic esterification in organic media: role of water and organic solvent in kinetics and yield of butyl butyrate synthesis

Summary The respective roles of organic solvent and of water in butyl butyrate synthesis from n-butanol and n-butyric acid in n-hexane by Mucor miehei lipase have been investigated by analysis of the kinetics and the reaction balances. Esterificaton was found to take place in both low water systems containing solid enzyme in hexane and in biphasic aqueous enzyme solution/hexane systems. In the solid enzyme system, the enzyme adsorbed the water produced, thus delaying the appearance of a discrete aqueous phase. As expected, the presence of some water was indispensable for this system, as its removal or exclusion by various means (adsorption, distillation) affected enzyme activity. However, water removal had little effect on the final yield of esterification. Reaction velocities were quite similar for the solid enzyme/hexane system and for the biphasic aqueous enzyme solution/hexane system. In the latter case, the butyl butyrate formed was almost exclusively found in the organic phase. Ethyl butyrate, a more polar compound, was synthesized with a lower yield. These results allow the conclusion that the reaction took place in a phase consisting of either solid hydrated enzyme with no discrete aqueous phase or of an aqueous enzyme solution by basically similar mechanisms according to the amount of water available to the system, the esterification being driven to completion by transfer of the ester into the organic phase because of a favourable partition coefficient. Offprint requests to: F. Monot     

Alcalase-catalyzed, kinetically controlled synthesis of a precursor dipeptide of RGDS in organic solvents

The protease-catalyzed, kinetically controlled synthesis of a precursor dipeptide of RGDS, Z-Asp-Ser-NH2 in organic solvents was studied. Alcalase, an industrial alkaline protease, was used to catalyze the synthesis of the target dipeptide in water-organic cosolvents systems with Z-Asp-OMe as the acyl donor and Ser-NH2 as the nucleophile. Acetonitrile was selected as the organic solvent from acetonitrile, ethanol, methanol, DMF, DMSO, ethyl acetate, 2-methyl-2-propanol, and chloroform tested under the experimental conditions. The conditions of the synthesis reaction were optimized by examining the effects of several factors, including water content, temperature, pH, and reaction time on the Z-Asp-Ser-NH2 yields. The optimum conditions are pH 10.0, 35 degrees C, in acetonitrile/Na2CO3-NaHCO3 buffer system (85:15, v/v), 6 h, with a dipeptide yield of 75.5%.