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.     

Peptide synthesis enzymatically catalyzed in a biphasic system: Water–water–immiscible organic solvent

Synthesis of a peptide bond is suggested to be enzymatically catalysed in a biphasic system “water–water-immiscible organic solvent”. The pH dependence of the apparent equilibrium constant is studied for synthesis of N-acetyl-L -tryptophanyl-L -leucine amide from N-Acet-Trp andL -Leu-NH₂. The reaction was performed in the biphasic system ethyl acetate plus water [from 2 to 2% (v/v)] in the presence of α-chymotrypsin. The suggested approach is preparative value: with the stoichiometric ratio of the reagents, [N-Acet-L -Trp] = [L -Leu-NH₂] = 2 × 10^?3M, the yield is practically 100% (in water, with other conditions being the same, the yield is not over 01.%).     

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.     

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.     

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 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     

Enzymatic Synthesis of N-formyl-L-aspartyl-L-phenylalanine Methyl Ester (Aspartame Precursor) Utilizing an Extractive Reaction in Aqueous/Organic Biphasic Medium

N-Formyl-L-aspartyl-L-phenylalanine methyl ester (N-formyl aspartame, F-AspPheOMe) was synthesized enzymatically utilizing an extractive reaction in an aqueous/organic biphasic system. The N-formyl aspartame yield in a pure aqueous monophasic system was, in general, ca. 3% , however, it was over 80 % in a water/1-butanol biphasic system using a simultaneously extractive operation of an enzymatic reaction in an aqueous phase and a product separation from an aqueous to an organic phases.     

Biphasic one-pot synthesis of two useful and separable compounds using nicotinamide cofactor-requiring enzymes: Syntheses of (S)-4-hydroxyhexanoate and its lactone

Several one-pot syntheses of two valuable and separable compounds in a biphasic system using nicotinamide cofactor-requiring enzymes are described. In this system, two synthetic reactions occur in the aqueous phase where the N AD or N ADP cofactor is recycled ≈ 1000 times, and the reduction product is extracted into the organic phase while the oxidation product is retained in the aqueous phase. The effective separation of products and elimination of product inhibition during the reaction makes the biphasic system practical for large-scale synthesis. Several chiral hydroxy compounds of synthetic value have been prepared. Manipulation of N AD-dependent enzymes in synthesis in water-immiscible organic solvent by entrapment of both enzyme and the cofactor in X AD-8 is described.     

Enhancing productivity for cascade biotransformation of styrene to (S)-vicinal diol with biphasic system in hollow fiber membrane bioreactor

Biotransformation is a green and useful tool for sustainable and selective chemical synthesis. However, it often suffers from the toxicity and inhibition from organic substrates or products. Here, we established a hollow fiber membrane bioreactor (HFMB)-based aqueous/organic biphasic system, for the first time, to enhance the productivity of a cascade biotransformation with strong substrate toxicity and inhibition. The enantioselective trans-dihydroxylation of styrene to (S)-1-phenyl-1,2-ethanediol, catalyzed by Escherichia coli (SSP1) coexpressing styrene monooxygenase and an epoxide hydrolase, was performed in HFMB with organic solvent in the shell side and aqueous cell suspension in the lumen side. Various organic solvents were investigated, and n-hexadecane was found as the best for the HFMB-based biphasic system. Comparing to other reported biphasic systems assisted by HFMB, our system not only shield much of the substrate toxicity but also deflate the product recovery burden in downstream processing as the majority of styrene stayed in organic phase while the diol product mostly remained in the aqueous phase. The established HFMB-based biphasic system enhanced the production titer to 143 mM, being 16-fold higher than the aqueous system and 1.6-fold higher than the traditional dispersive partitioning biphase system. Furthermore, the combination of biphasic system with HFMB prevents the foaming and emulsification, thus reducing the burden in downstream purification. HFMB-based biphasic system could serve as a suitable platform for enhancing the productivity of single-step or cascade biotransformation with toxic substrates to produce useful and valuable chemicals.

     

Urease-catalyzed urea synthesis.

The equilibrium of hydrolytic reactions can be shifted toward condensation by carrying out the reaction at low water concentration. The rate and yield of urease-catalyzed urea synthesis from (NH₄)₂CO₃ or NH₄HCO₃ has been examined as a function of water concentration (in mixtures with organic solvents), substrate and H⁺ concentration, and polarity of the nonaqueous component of the solvent. Similar effects of organic solvents are observed on the reaction rate in both directions; the results suggest that at least in some conditions the reaction proceeds through nonenzymically formed carbamate. The equilibrium concentration of urea, in 50% ($\text{v}\text{v}$) water, varies over 10-fold, depending on the nature of the nonaqueous component of the solvent; nonhydroxylic solvents such as acetone given the highest yield. Solubility measurements suggest that the interactions of the solvent mixtures with (NH₄)₂CO₃ (or carbamate), rather than urea, are responsible for the variations in urea yield. Activities of water and the ionic components of the equilibrium are strongly influenced by the nature of the nonaqueous component of the solvent, as well as its concentration.     

Temperature optima of enzyme-catalysed reactions in microemulsion systems

Ternary phase systems (water/surfactant/organic solvent) were utilised to increase and broaden the temperature optima of enzyme-catalysed reactions. Alcohol dehydrogenases from yeast and Thermoanaerobium brockii (EC 1.1.1.1 and EC 1.1.1.2), lactate dehydrogenase from Lactobacillus delbrueckii (EC 1.1.1.28) and the particulate hydrogenase from Ralstonia eutropha (EC 1.18.99.1) were used as model enzymes in microemulsions, consisting of the surfactant Aerosol OT, and various alkane solvent and aqueous phases. All enzymes exhibited, besides an increase in specific activity, an upshift of the temperature optimum of the catalysed reaction. The temperature optimum could be further shifted by variation of the chain length of the solvent used and/or the addition of compatible solutes to the aqueous phase. Under optimised conditions, catalytic reactions of enzymes from mesophilic microorganisms had temperature optima in the range generally obtained with enzymes from thermophilic organisms.     

Preparative separation of the saponin lancemaside a from Codonopsis lanceolata by centrifugal partition chromatography

Introduction. Lancemaside A is a saponin that inhibits decreases in blood testosterone level and thus prevents or ameliorates symptoms associated with male climacteric disorder. Our initial attempt to preparative isolation of lancemaside A from the saponin fraction of Codonopsis lanceolata roots by a preparative HPLC did not give a clear result. Objective. To develop a simple and efficient method for the preparative isolation of lancemaside A from the hot water extract of C. lanceolata roots using centrifugal partition chromatography (CPC). Methodology. The saponin fraction obtained from the hot water extract of C. lanceolata roots was used as the sample for preparative‐scale separation of lancemasides by CPC using n‐hexane:n‐butanol:methanol:0.1% aqueous formic acid (3:4:1:6, v/v) as the two‐phase solvent system. The upper phase (organic phase) of the two‐phase solvent system was used as the mobile phase, and 0.5 g of saponin fraction was applied for separation by CPC. Each fraction that was separated by CPC was analysed by HPLC, and the fractions containing each of the separated compounds were pooled together, and then were purified by simple preparative HPLC. Results. The demonstrated separation sequence, hot water extraction, DIAION HP‐20 column chromatography, CPC and preparative HPLC, yielded lancemaside A, foetidissimoside A and astersaponin Hb in their pure forms. Conclusion. The simple and efficient method for the preparative isolation of lancemaside A along with two other saponins, foetidissimoside A and astersaponin Hb, from the saponin fraction of C. lanceolata was established using CPC.     

Mass transfer induced interchange of the kinetic and thermodynamic control of enzymic peptide synthesis in biphasic water-organic systems

The α-chymotrypsin catalysed kinetically controlled peptide synthesis in water and in biphasic water-methyl iso-butyl ketone system was compared. Due to the substrate and product partitioning in the biphasic system an interchange of the reaction control was observed at high enzyme concentration. Under these conditions, the rate of mass transfer between the phases was the rate limiting step and the hydrolysis product concentration was found to have a transient maximum ≫ equilibrium value. In this case, most of the peptide was sythetized in a thermodynamically controlled process. In an aqueous one phase system, the peptide synthesis was kinetically controlled.     

低水有机介质中的酶催化

酶不仅能在水溶液里催化化学反应,而且能在有机介质中显示催化活性．其中低水溶剂体系对有机合成最为有利．文章就低水溶剂体系中影响酶催化的三要素（水、溶剂和载体）以及酶在该体系表现出来的一些特殊性质进行了讨论,并列举了低水溶剂体系中的酶催化在有机合成,化学分析,和高分子化学等方面的应用．     

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.     

A three-dimensional solubility parameter approach to nonaqueous enzymology

Widespread commercial application of enzymes as catalysts for specialty or commodity chemical synthesis will require their use in nonaqueous systems. While a number of non-aqueous enzyme applications have been demonstrated, the lack of useful rules for predicting enzyme-solvent interactions has hindered the development of this technology. Both Hildebrand and solvent hydrophobicity (octanol-water partition coefficient) parameters have been used previously to correlate and predict enzyme activity in nonaqueous systems, with some success, but any single-parameter approach is inherently limited in its ability to reflect the spectrum of possible enzyme-solvent interactions. Therefore, this study evaluates the three-dimensional solubility parameter space, as proposed by Hansen, to correlate and predict enzyme activity in microaqueous, miscible, and biphasic nonaqueous systems. Preliminary results suggest that Hansen parameters may be useful for correlating nonaqueous enzyme activity, and that the dispersive and polar parameters may be disproportionately important in single-phase microaqueous systems. The Hansen hydrogen-bonding parameter appears to be the only parameter yet evaluated capable of correlating the water requirement for enzyme activity in microaqueous systems, suggesting that water affects protein structure through enthalpic rather than entropic processes in nonaqueous systems. Insufficient data are available for miscible and biphasic systems, but it is proposed that enzyme activity may correlate with the average solubility parameters of miscible systems and of the aqueous phase in biphasic systems.     

Enhanced biodegradation of phenanthrene in a biphasic culture system

Degradation of phenanthrene byPseudomonas aeruginosa AK1 was examined in (i) an aqueous mineral salts medium to which phenanthrene particles of varying size (i.e. diameter) were added, and (ii) an aqueous/organic biphasic culture system consisting of mineral salts medium supplemented with 2,2,4,4,6,8,8-heptamethylnonane (HMN) as the phenanthrene-carrying organic phase. In both systems, the rate of phenanthrene biodegradation could be significantly enhanced by manipulations leading to improved phenanthrene mass transfer into the aqueous phase. With crystalline phenanthrene, the rate of biodegradation was found to be directly correlated to the particle surface area, whereas in the biphasic system the rate of biodegradation of the dissolved phenanthrene was mainly governed by the HMN/water interface area. In the latter system, exponential growth with a doubling time t _d of 6–8 hours has been achieved under conditions of intensive agitation of the medium indicating that phenanthrene degradation by strain AK1 is limited mainly by physicochemical parameters. Addition of selected surfactants to the culture medium was found to accelerate phenanthrene degradation by strain AK1 only under conditions of low agitation (in the presence of HMN) and after pretreatment of phenanthrene crystals by ultrasonication (in the absence of HMN). Evidence is presented that the stimulating effect of the surfactants was primarily due to improved dispersion of phenanthrene particle agglomerates (in the aqueous mineral salts medium supplemented with phenanthrene crystals) or of the phenanthrene-carrying lipophilic solvent drops (in the aqueous/organic biphasic culture system) whereas the solubilizing activity towards phenanthrene was neglectible. Under conditions of intensive mixing of the culture medium (i.e. if a high particle surface area or HMN/water interface area, respectively, is provided), the addition of surfactants did not enhance phenanthrene biodegradation.     

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.     

Enzyme activation for organic solvents made easy

Enzymes are highly selective catalysts that perform intricate chemistries at ambient temperatures and pressures. Although water is the solvent of life, it is a poor solvent for most synthetic organic reactions and, therefore, most chemists avoid aqueous solutions for synthetic applications. However, when removed from the aqueous environment and placed in an organic solvent, enzyme activity is reduced greatly. Here, we present a general overview of recent efforts to activate enzymes for use in nonaqueous media, giving particular focus to the use of simple salts as additives that result in significant biocatalytic improvements.     

A mathematical model for the synthesis of Gly-Phe by papain in an aqueous-organic system

The synthesis of the protected dipeptide BocGlyPheOMe, has been modellised when working in an aqueousorganic biphasic system, with papain as a catalyst. The mathematical model takes into account that one of the substrates, PheOMe, has parallel hydrolysis reactions and that the reaction only takes place in the aqueous phase while the whole reaction system is biphasic. The reaction system has been modellised when working in batch as well as when working in fed-batch mode, achieving a good prediction of the product evolution for both working strategies. When working in fed-batch mode, the extension of the undesired parallel reactions has been diminished, the model has been used for a computer aided optimisation of the addition sequence of PheOMe. The results obtained led to a process operation strategy with a compromise between yield and productivity.List of Symbols [i] concentration of any component i - [i] _aq concentration of i in the aqueous phase - [i] _bi concentration of i in the biphasic system - [E] ₀ initial concentration of enzyme - k _e, k_q first order kinetic constants - K _A, K_B equilibrium constants - r _m maximum rate of reaction This worked was financed by the Interministerial Commission for Science and Technology (CICYT)from the Spanish Government under projects number BIO/88-370 and SAF92-0261-CO2-02.