Kinetic resolution of rac-alkyl alcohols via lipase-catalyzed enantioselective acylation using succinic anhydride as acylating agent

With succinic anhydride as acylating agent, three commercial lipases – Candida antarctica lipase B (CALB), Pseudomonas cepacia lipase and Pseudomonas fluorescens lipase – were employed in the kinetic resolution of a series of rac-alkyl alcohols: 2-butanol, 2-pentanol, 2-hexanol, 2-heptanol, 2-octanol, 3-hexanol, 3-methyl-2-butanol, 6-methyl-5-heptene-2-ol, 3-methyl-2-cyclohexene-1-ol and 2-methyl-1-pentanol. The most effective tested enzyme, immobilized CALB, was able to resolve most of the alcohols with high enantioselectivity, even higher (with enantiomeric ratios up to 115 and 91, for 3-hexanol and 3-methyl-2-butanol, respectively) than when vinyl acetate was used as the acylating agent. More importantly, the unreacted alcohol and the monoester succinate produced could be easily separated by a simple aqueous base-organic solvent liquid–liquid extraction. Using succinic anhydride as acylating agent and CALB, enantiomerically pure (S)-2-pentanol with 99% ee and (R)-2-pentanol with 95% ee were prepared in gram-scale reactions.     

Enantioselective synthesis of (S)-ibuprofen ester prodrug in cyclohexane by Candida rugosa lipase immobilized on Accurel MP1000

An enantioselective esterification process was developed for the synthesis of 2-N-morpholinoethyl (S)-ibuprofen ester prodrug from racemic ibuprofen by using Candida rugosa lipase immobilized on Accurel MP1000 in cyclohexane. Compared with the performance of Lipase MY, the immobilized lipase possesses a higher enzyme activity and thermal stability, but with a slightly suppressed enantioselectivity. A kinetic model was proposed and confirmed from experiments, for the simulation of time-course conversions of both enantiomers at various combinations of substrate concentrations in a batch reactor. Preliminary results of employing the proposed model and the immobilized lipase in a continuous packed-bed reactor were also reported and discussed.     

Enzymatic kinetic resolution of racemic ibuprofen: past,present and future

This review is a journey concerning the investigations of the kinetic resolution of racemic ibuprofen for the last 20 years. The relevancy of the pharmacological uses of the S(?+?) enantiomer along with its higher cost compared with racemic profen are the driving forces of a variety of scientific research studies addressing the enzymatic resolution of ibuprofen through enantiomeric esterification using lipases as biocatalysts. Lipases of fungal sources such as Candida rugosa, Rhizomucor miehei and the lipase B of Candida antarctica have been extensively studied both in homogeneous and heterogeneous (immobilized on solid supports) processes. In this context, the various alcohols and organic co-solvents frequently used in the esterification of racemic ibuprofen are summarized and discussed in this review. Moreover, recent investigations using membranes as reactors coupled with the separation of the desired product and microfluidic devices are presented. Finally, some guidelines about future perspectives regarding the technology of the kinetic resolution of profens and research niches are given.     

Kinetic Analysis and Simulation Studies for Lipase-Catalysed Resolution of Racemic 2-Methyl-1-Pentanol

The lipase-catalysed optical resolution of a racemic mixture of 2-methyl-l-pentanol by transesterifica-tion using vinyl acetate as acyl donor has been studied experimentally. A mechanistic model has been developed for the double-substrate reaction sequence treating both enantiomers as competing substrates. The model is based upon a ping-pong mechanism with alternative substrates involving an acyl-enzyme intermediate. The kinetic constants of the model have been evaluated using initial rate experiments and nonlinear regression analysis. The model successfully predicts the evolution of the enantiomeric excess of substrate (ee_R) and the degree of conversion with time for batch experiments with various initial concentrations of vinyl acetate and (R,S)-2-methyl-1-pentanol. Furthermore, the rate equations have been used to theoretically study the dynamic progression of a continuous enzyme-catalysed resolution process. The enantiomeric excess as a function of conversion for different process configurations is discussed. It is found, that the maximum attainable ee_R is strongly dependent on the residence time distribution of the continuous reactor and is rather low for a continuous stirred tank reactor (CSTR) due to competitive inhibition effects.     

Kinetics of lipase-catalyzed esterification in supercritical CO(2)

This study compares two solvents for enzymatic reactions: supercritical carbon dioxide (SCCO(2)) and organic solvent (n-hexane). The model reaction that was chosen was the esterification of oleic acid by ethanol catalyzed by an immobilized lipase from Mucor miehei (Lypozyme). The stability of the enzyme appeared to be quite good and similar in both media but was affected by the water content. Partition of water between solvents and immobilized enzyme has been calculated from experimental adsorption isotherms. The water content of the solid phase has a dramatic influence on the activity of the enzyme and its optimum value for activity was about 10% (w/w) in both media. A kinetic study enabled a Ping-Pong Bi-Bi reaction mechanism with inhibition by ethanol to be suggested. Despite some differences in kinetic constants, activity was in the same range in both media. Hypotheses for explaining the kinetic constant variations have been proposed and particular attention has been paid to the pH effects.     

Enhanced activity and enantioselectivity of Candida rugosa lipase immobilized on macroporous adsorptive resins for ibuprofen resolution

The lipase from Candida rugosa was immobilized on three commercially available macroporous adsorptive resins for kinetic resolution of ibuprofen. One resin, CRB02, increased the enzyme activity by 50% to 0.027 g g(-1) min(-1). The deactivation constant (0.19 h(-1)) of the immobilized enzyme was half of that of the native enzyme and the enantioselectivity (E = 29.2) of the immobilized lipase was 2.2 times as much as that of the native lipase for the kinetic resolution of ibuprofen with 1-propanol in isooctane at 30 degrees C.     

Batch reactor performance for the enzymatic synthesis of cephalexin: influence of catalyst enzyme loading and particle size

A mathematical model is presented for the kinetically controlled synthesis of cephalexin that describes the heterogeneous reaction-diffusion process involved in a batch reactor with glyoxyl-agarose immobilized penicillin acylase. The model is based on equations considering reaction and diffusion components. Reaction kinetics was considered according to the mechanism proposed by Schro?n, while diffusion of the reacting species was described according to Fick's law. Intrinsic kinetic and diffusion parameters were experimentally determined in independent experiments. It was found that from the four kinetic constants, the one corresponding to the acyl-enzyme complex hydrolysis step had the greatest value, as previously reported by other authors. The effective diffusion coefficients of all substances were about 5×10(-10)m(2)/s, being 10% lower than free diffusion coefficients and therefore agreed with the highly porous structure of glyoxyl-agarose particles. Simulations made from the reaction-diffusion model equations were used to evaluate and analyze the impact of internal diffusional restrictions in function of catalyst enzyme loading and particle size. Increasing internal diffusional restrictions decreases the Cex synthesis/hydrolysis ratio, the conversion yield and the specific productivity. A nonlinear relationship between catalyst enzyme loading and specific productivity of Cex was obtained with the implication that an increase in catalyst enzyme loading will not increase the volumetric productivity by the same magnitude as it occurs with the free enzyme. Optimization of catalyst and reactor design should be done considering catalyst enzyme loading and particle size as the most important variables. The approach presented can be extended to other processes catalyzed by immobilized enzymes.     

Surfactant enhancement of (S)-naproxen ester productivity from racemic naproxen by lipase in isooctane

In the enantioselective esterification of racemic Naproxen with trimethylsilyl methanol in isooctane by Candida cylindracea lipase, improvements in (S)-naproxen ester productivity and enzyme selectivity were demonstrated by adding bis(2-ethylhexyl) sodium sulfosuccinate (AOT) as the best surfactant. The effect of water content on the enhancement of enzyme activity was elucidated from the reduced adsorption of surfactant molecules on the lipase. A competitive inhibition by the alcohol and a noncompetitive inhibition by the surfactant to the enzyme were found from the kinetic analysis. By using a two-phase extraction, a complete separation of the surfactant from the organic solution was obtained. (c) 1996 John Wiley & Sons, Inc.     

Enantioselective lipase-catalyzed kinetic resolution of N-(2-ethyl-6-methylphenyl)alanine

The enzyme (BSL2), a highly active lipase expressed from newly constructed strain of Bacillus subtilis BSL2, is used in the kinetic resolution of N-(2-ethyl-6-methylphenyl)alanine from the corresponding racemic methyl ester. Reaction conditions are optimized to enhance the enantioselectivity. The effects of various racemic alkyl esters, substrate concentration, operating temperature, pH of the aqueous medium and organic solvents on activity and enantioselectivity of BSL2 for kinetic resolution are also studied. A high enantiomeric ratio (E = 60.7) is reached in diisopropyl ether/water (10%, v/v) and the enantioselectivity is about 22-fold higher than that in pure buffered aqueous solution. The results show that the reaction medium greatly influences BSL2 reaction and its enantioselectivity in the hydrolysis of racemic methyl ester.     

Investigations of reaction kinetics for immobilized enzymes--identification of parameters in the presence of diffusion limitation

A method is proposed for identification of kinetic parameters when diffusion of substrates is limiting in reactions catalyzed by immobilized enzymes. This method overcomes conventional sequential procedures, which assume immobilization does not affect the conformation of the enzyme and, thus, consider intrinsic and inherent kinetics to be the same. The coupled equations describing intraparticle mass transport are solved simultaneously using numerical methods and are used for direct estimation of kinetic parameters by fitting modeling results to time-course measurements in a stirred tank reactor. While most traditional procedures were based on Michaelis-Menten kinetics, the method presented here is applicable to more complex kinetic mechanisms involving multiple state variables, such as ping-pong bi-bi. The method is applied to the kinetic resolution of (R/S)-1-methoxy-2-propanol with vinyl acetate catalyzed by Candida antarctica lipase B. A mathematical model is developed consisting of irreversible ping-pong bi-bi kinetics, including competitive inhibition of both enantiomers. The kinetic model, which fits to experimental data over a wide range of both substrates (5-95%) and temperatures (5-56 degrees C), is used for simulations to study typical behavior of immobilized enzyme systems.     

Cross-linked enzyme aggregates (CLEAs) with controlled particles: Application to Candida rugosa lipase

Aggregation agent type and concentration, lipase and glutaraldehyde concentration, and pH are able to affect the formation of cross-linked lipase. The carrier-free immobilized Candida rugosa lipase with a particle size of 40–50 μm showed higher activity than that of the lipase with other particle sizes. The carrier-free immobilized C. rugosa lipase can keep 86% original lipase activity (0.018 g g⁻¹ min⁻¹). The enantioselectivity of the carrier-free immobilized lipase (23.3) was about 1.8 times as much as that of the native lipase (13.0) in kinetic resolution of ibuprofen racemic mixture.     

Effect of the hydration state of supports before lyophilization on subtilisin-A activity in organic media

Subtilisin-A was colyophilized with various types of support materials, such as Amberlite IRC-50, Celite545, chitosan, DEAE-cellulose, DOWEX-1, zeolite, glass bead, and polystyrene. The colyophilized enzyme was used for the optical resolution of racemic 1-phenylethylamine with 2,2,2-trifluoroethylbutyrate in 3-methyl-3-pentanol. The enzyme activity in organic media changed dramatically according to the hydration state of the support materials before lyophilization. This effect was especially marked with supports of high water capacity (aquaphilicity), such as chitosan and DEAE-cellulose. By hydrating these supports of high aquaphilicity prior to lyophilization, subtilisin-A activity in organic media increased ca. 4-8 times, depending upon the supports used. This result suggests that the hydration state of aquaphilic support materials for colyophilization is critical to determining enzyme activity in organic solvents. (c) 1996 John Wiley & Sons, Inc.     

Enantioselective preparation of (R) and (S)-3-hydroxycyclopentanone by kinetic resolution

A straightforward approach to enantiomerically enriched (R) and (S)-3-hydroxycyclopentanone is described. The key step involves a kinetic resolution of racemic 3-hydroxycyclopentanone using commercial Pseudomonas cepacia lipase immobilized on diatomite (Amano lipase PS-DI). The absolute stereochemistry of the product was determined by derivatization into (R)-3-(benzyloxy)cyclopentanone.     

Effect of mass transfer limitations on the enzymatic kinetic resolution of epoxides in a two-liquid-phase system

Optically active epoxides can be obtained by kinetic resolution of racemic mixtures using enantioselective epoxide hydrolases. To increase the productivity of the conversion of sparingly aqueous soluble epoxides, we investigated the use of a two-phase aqueous/organic system. A kinetic model which takes into account interphase mass transfer, enzymatic reaction, and enzyme inactivation was developed to describe epoxide conversion in the system by the epoxide hydrolase from Agrobacterium radiobacter. A Lewis cell was used to determine model parameters and results from resolutions carried out in the Lewis cell were compared to model predictions to validate the model. It was found that n-octane is a biocompatible immiscible solvent suitable for use as the organic phase. Good agreement between the model predictions and experimental data was found when the enzyme inactivation rate was fitted. Simulations showed that mass transfer limitations have to be avoided in order to maximize the yield of enantiomerically pure epoxide. Resolution of a 39 g/L solution of racemic styrene oxide in octane was successfully carried out in an emulsion batch reactor to obtain (S)-styrene oxide in high enantiomeric excess (>95% e.e.) with a yield of 30%.     

Solvent as a competitive inhibitor for Candida antarctica lipase B

In enzyme-catalyzed reactions, the choice of solvent often has a marked effect on the reaction outcome. In this paper, it is shown that solvent effects could be explained by the ability of the solvent to act as a competitive inhibitor to the substrate. Experimentally, the effect of six solvents, 2-pentanone, 3-pentanone, 2-methyl-2-pentanol, 3-methyl-3-pentanol, 2-methylpentane and 3-methylpentane, was studied in a solid/gas reactor. As a model reaction, the CALB-catalyzed transacylation between methyl propanoate and 1-propanol, was studied. It was shown that both ketones inhibited the enzyme activity whereas the tertiary alcohols and the hydrocarbons did not. Alcohol inhibition constants, K(i)(I) were changed to "K(i)", determined in presence of 2-pentanone, 3-pentanone, and 3-methyl-3-pentanol, confirmed the marked inhibitory character of the ketones and an absence of inhibition of 3-methyl-3-pentanol. The molecular modeling study was performed on three solvents, 2-pentanone, 2-methyl-2-pentanol and 2-methyl pentane. It showed a clear inhibitory effect for the ketone and the tertiary alcohol, but no effect for the hydrocarbon. No change in enzyme conformation was seen during the simulations. The study led to the conclusion that the effect of added organic component on lipase catalyzed transacylation could be explained by the competitive inhibitory character of solvents towards the first binding substrate methyl propanoate.     

Study of the resolution of amino acids and aminoalcohols in organic solvents

Summary The enzymatic resolution of racemic phenylglycine, phenylglycinol and phenylalaninol has been studied in organic solvents under a variety of experimental conditions. Subtilisin in 3-methyl-3-pentanol was effective for the resolution of phenylglycine esters, via N-acylation with trifluoroethyl butyrate. Porcine pancreatic lipase in ethyl acetate gave satisfactory results in the resolution of phenylglycinol and phenylalaninol; the or position of the phenyl group was found to influence both the rate and the chemioselectivity of the reaction.     

Impressive effect of immobilization conditions on the catalytic activity and enantioselectivity of Candida rugosa lipase toward S-Naproxen production

Candida rugosa lipase (CRL) was immobilized on Amberlite XAD 7 and the advantage of immobilization under the best reaction conditions in achieving high activity and enantioselectivity was shown for the hydrolysis of racemic Naproxen methyl ester. The performance of CRL was found to be better when the enzyme was immobilized at the temperature and pH values where higher conversion and enantioselectivity were obtained. The effects of immobilized lipase load, temperature, pH and substrate concentration on the conversion and enantioselectivity toward S-Naproxen production in aqueous phase/isooctane biphasic batch system were also evaluated. The increase in immobilized lipase load in 320–800 U/mL range increased the conversion of the substrate and enantioselectivity for S-Naproxen. The kinetic resolution of racemic Naproxen methyl ester conducted at the temperatures of 40, 45 and 50 °C and at the pH values of 4, 6, 7.5 and 9 resulted in the highest conversion and enantioselectivity at 45 °C and pH 6. Higher concentration of racemic Naproxen methyl ester than 10 mg/mL decreased both the conversion and enantioselectivity. CRL, which was immobilized at the temperature and pH values where the enzyme was more enantioselective, was successfully used in three successive batch runs each of 180 h. The highest enantiomeric ratio achieved in the S-Naproxen production was 174.2 with the conversion of 49%.     

Can an inactivating agent increase enzyme activity in organic solvent? Effects of 18‐crown‐6 on lipase activity,enantioselectivity, and conformation

Lipase from Burkholderia cepacia (lipase BC) and lipase B from Candida antarctica (CALB) show an increase of the transesterification activity in toluene (up to 2.4- and 1.7-fold, respectively), when lyophilized with 18-crown-6. Nevertheless, the increase was observed only for low (less than 100) 18-crown-6/lipase molar ratio, while at higher ratios, the activity decreased for both enzymes to values lower than those obtained in the absence of the additive. In 1,4-dioxane, the activation is lower for lipase BC (1.7-fold) and for CALB (1.5-fold). Concerning enantioselectivity, tested in the kinetic resolution of 6-methyl-5-hepten-2-ol, only in the case of CALB, an effect of the additive (the E value varied from about 120 to 280) was observed. In water, 4% (w/w) of 18-crown-6 caused a loss of activity in the hydrolysis of p-nitrophenyl laurate of about 88 and 99.75%, compared to that observed in the absence of the crown ether for CALB and lipase BC, respectively. These data and the conformational analysis of both lipases, carried out by FT/IR spectroscopy indicate that the enzyme inactivation in water and in organic solvents at 18-crown-6/lipase molar ratios, higher than 100 might be due to conformational changes caused by the additive. Instead, at molar ratios lower than 100, 18-crown-6 might increase the activity - particularly, in toluene - thanks to the fact that in its presence, the enzyme has an hydrogen bonds pattern, more similar to that in water. This suggests that the additive would be able to provide the enzyme with more water.     

Enantioselective esterification of butanol-2 in an enzyme membrane reactor

The enzymatic esterification of octanoic acid with racemic butanol-2 was investigated. Esterifications of the acid were performed in a forced flow enzyme membrane reactor. The used membrane was prepared by a phase inversion process in polyamide-6 solution followed by the chemical immobilization of a lipase-catalyst. Influences of water content and pH were estimated. Their optimum values are equal to 0.5% w/w and pH 8. The reaction rate (at 303 K) of 5.1 × 10^?5 mol/h·cm² of the membrane area, and at least 85% enantiomeric excess in the produced ester mixture were obtained. The activity of immobilized lipase in the membrane process is about two times higher than that of the native lipase in the esterification performed in a tank reactor.     

Study of lipase immobilization on zeolitic support and transesterification reaction in a solvent free-system

In order to understand the role of the acid–base, electrostatic and covalent interactions between enzyme and support, the catalytic behavior of the Rhizomucor miehei lipase (RML) immobilized on zeolite materials has been studied. The highest lipase activities were obtained when this enzyme, immobilized by adsorption, interacts through acid–base binding forces with the support surface, resulting in activation of the enzyme catalytic center. Due to the interest in biodiesel production by mild enzymatic transesterification, this heterogeneous biocatalyst has been used in transesterification of fatty acids contained in olive oil. The results show a high oleic acid conversion for several reaction cycles with a higher total biodiesel productivity compared to that using the free enzyme.