Alcoholysis catalyzed by Candida antarctica lipase B in a gas/solid system: effects of water on kinetic parameters

The influence of water on the kinetics of alcoholysis of methyl propionate and n-propanol catalyzed by immobilized lipase B from Candida antarctica was studied in a continuous solid/gas reactor. In this reactor, the solid phase is composed of a packed enzymatic sample which is percolated by gaseous nitrogen, simultaneously carrying gaseous substrates to the enzyme while removing reaction products. In this system, interactions between the enzyme and nonreacting molecules are avoided, since no solvent is present, and it is thus more easy to assess the role of water. To this end, alcohol inhibition constant, substrates dissociation constants as well as acylation rate constant and ratio of acylation to deacylation rate constants have been determined as a function of water activity (a(w)). Data obtained highlight that n-propanol inhibition constant and dissociation constant of methyl propionate are a lot affected by a(w) variations whereas water has no significant effect on the catalytic acylation step nor on the ratio of acylation to deacylation rate constants. These results suggest the water-independent character of the transition step.     

Water plays a different role on activation thermodynamic parameters of alcoholysis reaction catalyzed by lipase in gaseous and organic media

The effect of water on the alcoholysis of methyl propionate and n-propanol catalyzed by immobilized Candida antarctica lipase B (CALB) has been compared in a continuous solid-gas reactor and in an organic liquid medium. The enthalpic and entropic contributions of water to the Gibbs free energy of activation in the gas phase were different from the ones in the organic phase, the inverse trends being observed for the variation of both DeltaH* and DeltaS* with water activity.Different phenomena were identified for their influence on the thermodynamic parameters. When increasing a(w), the enhanced flexibility of the enzyme was predominant in the gas phase whereas substrate-solvent interactions due to an increased polarity of the solvent affected mainly the thermodynamic parameters in the organic phase. The observed variations of DeltaG* with water activity were in accordance with kinetics results previously obtained in both reaction media.     

Solid/gas biocatalysis: an appropriate tool to study the influence of organic components on kinetics of lipase-catalyzed alcoholysis

The influence of the addition of an extra component in a gaseous reaction medium, on the kinetics of alcoholysis of methyl propionate and n-propanol catalyzed by immobilized lipase B from Candida antarctica was studied in a continuous solid/gas reactor. In this reactor, the solid phase is composed of a packed enzymatic sample, which is percolated by gaseous nitrogen, simultaneously carrying gaseous substrates and additional components to the enzyme while removing reaction products. The system permits to set thermodynamic activity of all gaseous components (substrates or not) independently at the desired values. This allows in particular to study the influence of an extra added component at a constant thermodynamic activity value, contrary to classical solid/liquid system, which involves large variations of thermodynamic activity of added solvent, when performing full kinetic studies. Alcohol inhibition constant (K_I) and methyl propionate and propanol dissociation constants (K_MP and K_P) have been determined in the solid/gas reactor in the presence of 2-methyl-2-butanol, and compared with values previously obtained in the absence of added component and in the presence of water. Complementary experiments were carried out in the presence of an apolar compound (hexane) and led to the conclusion that the effect of added organic component on lipase-catalyzed alcoholysis is related to their competitive inhibitory character towards first substrate methyl propionate. The comparison of data obtained in liquid or with gaseous 2-methyl-2-butanol shows that lower K_MP and K_I are found in gaseous medium, which would correspond on the one hand to a lower acylation rate k₂, and on the other hand to a higher binding rate k₁ between substrate and free enzyme in gaseous medium.     

Kinetic studies of fusarium solani pisi cutinase used in a gas/solid system: transesterification and hydrolysis reactions

Fusarium solani cutinase supported onto Chromosorb P was used to catalyze transesterification (alcoholysis) and hydrolysis on short volatile alcohols and esters in a continuous gas/solid bioreactor. In this system, a solid phase composed of a packed enzymatic preparation was continuously percolated with carrier gas which fed substrates and removed reaction products simultaneously. A kinetic study was performed under differential operating conditions in order to get initial reaction rates. The effect of the hydration state of the biocatalyst on the kinetics was studied for 3 conditions of hydration (a(w) = 0.2, a(w) = 0.4 and a(w) = 0.6), the alcoholysis of propionic acid methyl ester with n-propanol, and for 5 hydration levels (from a(w) = 0.2 to a(w) = 0.6) for the hydrolysis of propionic acid methyl, ethyl or propyl esters. F. solani cutinase was found to have an unusual kinetic behavior. A sigmoid relationship between the rate of transesterification and the activity of methyl propionate was observed, suggesting some form of cooperative activation of the enzyme by one of its substrate. For the hydrolysis of short volatile propionic acid alkyl esters, threshold effects on the reaction rate, highly depending on the water activity and the substrate polarity, are reported. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 1-8, 1997.     

Gas phase transesterification reactions catalyzed by lipolytic enzymes

Porcine pancreatic lipase and Fusarium solani cutinase were used to catalyze transesterification reactions between methyl propionate, ethyl propionate, and a series of primary alcohols at high temperatures in a continuous packed-bed gas-solid reactor, in which the solid phase is composed of the enzyme and the substrates and products are in a gaseous form. In this type of system, enzyme activity was found to depend essentially on the water activity (A(w)) of the enzyme preparation.     

Study of vitamin ester synthesis by lipase-catalyzed transesterification in organic media

Immobilized lipase from Candida antarctica (Novozym 435) was used in organic media to catalyze esterifications of vitamins (ascorbic acid and retinol) from hydroxy acid. We described the synthesis of retinyl L-lactate by transesterification between retinol and L-methyl lactate with yield reaching 90% and the synthesis of ascorbyl L-lactate by transesterification between ascorbic acid and L-methyl lactate with yield reaching 80%. The kinetic study of the esterification of vitamins with L-methyl lactate in organic media has been carried out and agrees with ping-pong-ordered Bi-Bi when the initial vitamin concentration is low. When initial vitamin concentration is high, the kinetic is similar to a hybrid ping-pong-ordered Bi Bi or hybrid ping-pong-random Bi Bi mechanism. However, with high initial substrate concentration, change of the kinetic by other phenomena, such as interaction of substrates with molecular sieves, adsorption of the methanol formed, and decreases of substrate diffusion, could be considered. It is obvious that in these conditions, classical enzymology (i.e., Michaelian enzymology) cannot be used for the interpretation of results.     

脂肪酶在微乳液和微乳液凝胶中催化辛酸辛醇的酯化反应

脂肪酶在合成反应中具有很高的区域选择性和立体选择性 ,已广泛用于食品工业和药物工业[1,2 ] ,在有机介质中的脂肪酶催化反应已有较多研究[3 ,4 ] 。微乳液一般由表面活性剂、助表面活性剂、油和水等组份组成 ,它是一种热力学稳定、光学透明、宏观均匀而微观不均匀的体系 ,能提供酶催化所需要的巨大油 /水界面[5] 。而将脂肪酶增溶于油包水(Ｗ /Ｏ)微乳液中的纳米级“水池”中 ,可使酶以分子水平分散[6] ,图 1(ａ) ,从而可用来模拟细胞微环境中的反应。油包水微乳液中的酶可通过加入明胶而制成固定化酶 ,含明胶的微乳液凝胶 (ＭＢＧｓ)最早…     

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.     

Lipase-catalyzed enantioselective hydrolysis of methyl 2-fluoro-2-arylpropionates in water-saturated isooctane

Lipases from Candida rugosa, Candida antartica B and Carica papaya are employed as the biocatalyst for the hydrolytic resolution of methyl 2-fluoro-2-arylpropionates in water-saturated isooctane, in which excellent to good enantioselectivity without the formation of byproducts is obtained for the papaya lipase when using (R,S)-2-fluoronaproxen methyl ester (1) and methyl (R,S)-2-fluoro-2-(4-methoxyphenyl)propionate (2), but not methyl (R,S)-2-fluoro-2-(naphth-1-yl)propionate (3) as the substrates. The thermodynamic analysis indicates that the enantiomer discrimination for the papaya lipase is driven by the difference in activation enthalpy for compound 1, 2 or (R,S)-naproxen methyl ester (4). The kinetic analysis also demonstrates that in comparison with (S)-4, the insertion of the 2-fluorine moiety in (R)-1 has increased k₂, but not K_m, and consequently the lipase activity.     

Lipase-catalyzed transesterification in organic media: solvent effects on equilibrium and individual rate constants

The kinetics of the immobilized lipase B from Candida antarctica have been studied in organic solvents. This enzyme has been shown to be slightly affected by the water content of the organic media, and it does not seem to be subject to mass transfer limitations. On the other hand, some evidence indicates that the catalytic mechanism of reactions catalyzed by this lipase proceeds through the acyl-enzyme intermediate. Moreover, despite the fact that the immobilization support dramatically enhances the catalytic power of the enzyme, it does not interfere with the intrinsic solvent effect. Consequently, this enzyme preparation becomes optimum for studying the role played by the organic solvent in catalysis. To this end, we have measured the acylation and deacylation individual rate constants, and the binding equilibrium constant for the ester, in several organic environments. Data obtained show that the major effect of the organic solvent is on substrate binding, and that the catalytic steps are almost unaffected by the solvent, indicating the desolvation of the transition state. However, the strong decrease in binding for hydrophilic solvents such as THF and dioxane, compared to the rest of solvents, cannot be easily explained by means of thermodynamic arguments (desolvation of the ester substrate). For this reason, data have been considered as an indication of the existence of an unknown step in the catalytic pathway occurring prior to formation of the acyl-enzyme intermediate.     

Kinetics and specificity of serine proteases in peptide synthesis catalyzed in organic solvents

Initial rates of peptide-bond synthesis catalyzed by poly(ethylene glycol)-modified chymotrypsin in benzene were determined using high-performance liquid chromatography. Enzymatic synthesis of N-benzoyl-L-tyrosyl-L-phenylalanine amide from N-benzoyl-L-tyrosine ethyl ester and L-phenylalanine amide was found to obey Michaelis-Menten kinetics an to be consistent with a ping-pong mechanism modified by a hydrolytic branch. The catalytic activity of modified chymotrypsin was dependent on both water concentration and type of organic solvent, the highest synthesis rate being obtained in toluene. Since the chymotrypsin specificity in the organic phase was actually altered, the enzyme's apparent kinetic parameters were determined for different substrates and compared to those obtained with other serine proteases in benzene. Both N-benzoyl-L-tyrosine ethyl ester and N-alpha-benzoyl-L-lysine methyl ester were comparable acyl donors in benzene and the (kcat/Km)app value of modified chymotrypsin was only 10-fold smaller than that obtained with poly(ethylene glycol)-modified trypsin in the synthesis of N-alpha-benzoyl-L-lysyl-L-phenylalanine amide. The change in chymotrypsin specificity was also confirmed through the binding of trypsin inhibitors in benzene. The overall results suggest that hydrophobic bonding between the enzyme and its substrate should not be taken into account during catalysis in the organic phase. In general, if hydrophobic interactions are involved in the binding of substrates to the active site in aqueous media, the replacement of water by hydrophobic solvents will induce some change in enzyme specificity. Moreover, secondary residues of enzyme-binding sites may also exert a significant influence on specificity since, as observed in this study, chymotrypsin exhibited high affinity for cationic substrates and cationic inhibitors as well in apolar solvents.     

有机介质中脂肪酶催化外消旋苯甘氨酸甲酯的对映体选择性氨解反应

由水解酶催化的酯的对映体选择性水解和醇解反应 ,已在外消旋物质的拆分中得到广泛应用[1 ] 。近年来的一些研究表明 ,某些水解酶还可催化一些非天然酰基受体的转化 ,如过氧化氢、烷基胺、联胺和氨等。这些非天然酰基受体的转化反应在多肽的合成及手性化合物的拆分中显示出巨大的应用前景。其中 ,以氨为酰基受体的酶促氨解反应 ,是继酶促对映体选择性水解、酯化及转酯反应之后的另一制备光学纯化合物的新反应[2 ] 。目前国际上对这一新反应的研究尚属起步 ,国内未见有对该反应研究的报道。(Ｄ ,Ｌ) 苯甘氨酸是半合成 β 内酰胺类抗生素的重…     

Regioselective acylation of flavonoids catalyzed by immobilized Candida antarctica lipase under reduced pressure

A single-step acylation of rutin and naringin, catalyzed by immobilized Candida antarctica lipase B in 2-methyl-2-butanol, occurred preferentially on the primary hydroxyl group. Using palmitic methyl ester as acyl donor, the acylation rate of naringin was 10-fold higher than that of rutin. Under optimal conditions, i.e. a molar ratio acyl donor/naringin of 7:1 and 200 mbar, 92% naringin was acylated.     

R-stereopreference analysis of lipase Novozym 435 in kinetic resolution of flurbiprofen

Immobilized lipase from Candida antarctica (Novozym 435) was employed in the kinetic resolution of racemic flurbiprofen by enantioselective esterification with methanol. It was found that the lipase has the R-stereopreference and the reaction matches Bi Bi Ping Pong mechanism with dead-end inhibition of methanol. Furthermore, the R-stereopreference was analyzed in details from the aspects of enzymatic kinetic mechanism and reaction activation energy of both enantiomers. The R-enantiomer shows lower activation energy and higher maximum reaction rate than the S-enantiomer, which implies the R-stereopreference of the lipase and makes the kinetic resolution of flurbiprofen via enzymatic reaction feasible.     

A combinatorial biocatalysis approach to an array of cholic acid derivatives

A 39-member library of bile acid derivatives was prepared starting from 3alpha,7alpha,12alpha-trihydroxy-5beta-cholan-24-oic acid methyl ester using a combinatorial biocatalytic approach. A regioselective oxidation step, catalyzed by hydroxysteroid dehydrogenases, followed by an acylation step with a series of different acyl donors catalyzed by Candida antarctica lipase B, led to the modification of the bile acid scaffold. Each member of the library was obtained in high purity and good yield.     

Kinetic resolution of rac-2-pentanol catalyzed by Candida antarctica lipase B in the ionic liquid, 1-butyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]amide

The ionic liquid, l-butyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]amide ([Bmim] [NTf2]), was used as a reaction medium for the kinetic resolution of rac-2-pentanol catalyzed by free Candida antarctica lipase B, using vinyl propionate at 2% (v/v) water content. The synthetic activity of lipase in [Bmim] [NTf2] was up 2.5-times greater than in hexane, and showed high enantioselectivity (ee > 99.99%). The optimal temperature and pH were 60 degrees C and 7, respectively. A decrease in water activity (aw) produced a decay in synthetic activity, and an exponential increase in selectivity.     

Enzymatic acylation of hydroxypropyl cellulose in organic media and determination of ester formation by diffuse reflectance infrared Fourier transform (DRIFT) spectroscopy

Esters were prepared by acylation of hydroxypropyl cellulose with fatty acid catalyzed by immobilized lipase from Candida antarctica in tert-butanol. The nature of the substrates used, the initial water activity of the system, and the molecular weight of the hydroxypropyl cellulose were investigated. Moreover, Fourier transform-infrared (FT-IR) spectroscopy was used for determination of ester content on hydroxypropyl cellulose. Specifically, a linear relationship was established between the peak height assigned to the absorption of the esterified carboxyl groups of the cellulose and the ester content. At optimum reaction conditions, the ester content on the hydroxypropyl cellulose was about 11%.     

Lipase kinetics: hydrolysis of triacetin by lipase from Candida cylindracea in a hollow-fiber membrane reactor

The aptitude of a hollow-fiber membrane reactor to determine lipase kinetics was investigated using the hydrolysis of triacetin catalyzed by lipase from Canadida cylindracea as a model system. The binding of the lipase to the membrane appears not to be very specific (surface adsorption), and probably its conformation is hardly altered by immobilization, resulting in an activity comparable to that of the enzyme in its native form. The reaction kinetics defined on the membrane surface area were found to obey Michaelis-Menten kinetics. The specific activity of the lipase in the membrane reactor was found to be significantly higher than in an emulsion reactor. The activity and stability of the enzyme immobilized on a hydrophilic membrane surface seem not to be influenced significantly by the choice of the membrane material. The hollow-fiber membrane reactor is a suitable tool to assess lipase kinetics in a fast and convenient way.     

Substrate selectivity of lipases in the esterification of oleic acid, linoleic acid, linolenic acid and their all-trans-isomers and in the transesterification of cis/trans-isomers of linoleic acid methyl ester

The substrate selectivity of several microbial lipases has been examined in the esterification of oleic acid, linoleic acid, linolenic acid and their all-trans-isomers and in the alcoholysis of isomeric linoleic acid methyl esters with n-butanol. Lipases from Candida cylindracea and Mucor miehei preferred fatty acids and methyl esters with a (first) cis double bond in 9-position, while Chirazyme L-5, a Candida antarctica lipase A, had a preference for trans-9 unsaturated substrates.     

非水相中脂肪酶催化甘油三酯转酯反应动力学

本文研究了脂肪酶在己烷中催化甘油三丁酸酯与硬脂酸之间的转酯反应动力学。转酯反应分为二个连续的反应步骤:由酯生成的酰基酶复合物的水解和由酸生成的酰基酶复合物的醇解,整个反应符合乒乓反应机制,动力学参数为:K_m(酯)=3.2×10~(-2)mol/L,K_m(酸)=6.9×10~(-2)mol/L,V_m=1.7×10~(-4)mol/L·min。