Reaction equilibrium for lipase-catalyzed condensation in organic solvent systems

Lipase-catalyzed condensation in an organic solvent is useful for the syntheses of esters. To reasonably design and optimize the reaction conditions, knowledge of the reaction equilibrium is required. The interaction of water with other reactants and the quantitative predictions for adsorption of water by a desiccant are discussed. The solvent effects on the reaction equilibrium are also elucidated in mixtures of nitrile and tert-alcohol.     

Solvent effects on lipase-catalyzed esterification of glycerol and fatty acids

The lipase-catalyzed acylglycerol synthesis with fatty acids of different chain length is studied. Measured ester mole fractions at equilibrium are compared with calculated mole fractions. For these calculations the computer program TREP (Two-phase Reaction Equilibrium Prediction) is used. This program is based on the UNIFAC group contribution method and is developed for nondilute two-phase reaction systems.With one set of equilibrium constants, namely 1.3, 0.8, and 0.6 for monoester, diester, and triester synthesis, respectively, the equilibrium position of the reaction between glycerol and all saturated fatty acids with a chain length from 6 to 18 and oleic acid (cis-9-octadecenoic acid) can be calculated. Deviations, expressed as the ratio between calculated and measured ester mole fractions, usually were between 0.7 and 1.2. In the presence of solvents, the deviations of the monoester mole fractions were higher and rose up to 3. Without addition of a solvent, the ester mole fractions at equilibrium are dependent on the fatty acid chain length. With the short-chain hexanoic acid, the monoester mole fraction is the highest ester mole fraction, while for the long-chain oleic acid, the diester mole fraction is the highest one. The ester mole fractions become independent on the chain length of the fatty acid with a solvent added in a sufficient high concentration. Both reactions, with saturated and unsaturated C(18) fatty acids, lead to the same equilibrium position. The program TREP is found to make good predictions of the equilibrium amounts of ester and fatty acid. However, systematic deviations arise between measured and calculated amounts of water and glycerol in the organic phase. The calculated water and glycerol amounts are always lower than the measured ones. These deviations seem to be highest in nonpolar media and are probably due to deficiencies in the UNIFAC calculation method. Some preliminary experiments show the effect of the choice of solvent on the reaction rates. In polar solvents, the monoester production rate is enhances by a factor of 1.5 as compared to the reaction rate in a system without solvent. (c) 1993 John Wiley & Sons, Inc.     

The effect of organic solvents on the equilibrium position of enzymatic acylglycerol synthesis

The effect of organic solvents on the equilibrium position of lipase-catalyzed esterification of glycerol and decanoic acid has been investigated. The reaction is carried out in an aqueous-organic two-phase system. In polar solvents, high mole fractions of monoacylglycerol and low mole fractions of triacylglycerol and measured, while in nonpolar solvents, the measured differences in the mole fractions of monodi-, and triacylglycerols are less. There is a good correlation between the ester mole fractions at equilibrium and the log P of the solvent (partition coefficient in n-octanolwater), however, only if the group of tertiary alcohols is excluded. In the plot of the easter mole fractions as a function of the logarithm of hte solubility of water in the organic solvent, the tertiary alcohols can be included; however, in this case other deviations appear.For the prediction of the effect of organic solvents on the ester mole fractions at reaction equilibrium in nondilute reaction systems with a water activity below 1, the program TREP (Two-phase Reaction Equilibrium Prediction) is developed, which is based on the UNIFAC group contribution method. With this model the equilibrium data are essentially predicted from basic thermodynamic data. The required equilibrium constants are estimated from experiments without an organic solvent in the reaction medium. The mole fractions calculated by TREP show the same trends as the experimentally measured mole fractions; however, some variation is observed in the absolute values. These deviations may be due to inaccuracies in the UNIFAC group contribution method. TREP is found to be a correct method to predict within some limits the ester mole fractions at equilibrium for all mixtures of solvents, substrates, and products. The production of monoester can be enhanced in reaction system with a sufficient high concentration of a polar solvent. In experiments with a triglymeto-decanoic acid ratio of 5, almost no di-and triesters can be detected at equilibrium. (c) 1993 John Wiley & Sons, Inc.     

Continuous hydrolysis of olive oil by immobilized lipase in organic solvent

Lipase (EC 3.1.1.3) from Candida rugosa was immobilized with DEAE-Sephadex A50, Sephadex G50, Sephadex LH-20, Amberlite IRA94, and Amberlite XAD-7. The enzye immobilized with DEAE-Sephadex A50 was found to be most effective for continuous hydrolysis of olive oil in isooctane. For the continuous reaction, 0.2 g of dry immobilized enzyme was swollen with predetermined amount of water, and packed in a glass column reactor. When the organic solvent (Isooctane) containing olive oil substrate was cocurrently fed with aqueous buffer, the two phases were evenly distributed throughout the packed bed without surfactant supplement or prior mixing of the two phases. A small amount of the surfactant (AOT) was used only in packing procedure, and no additional surfactant was necessary thereafter. Effects of initial water content of the swollen gel, buffer types, and strength were examined in the continuous reaction. Our results suggest that the operational half-life was affected by desorption of the bound enzyme. Under the conditions of 20% olive oil in isooctane and 25 mM triethanolamine buffer (pH 7.0), operational half life was 220 h at 30 degrees C. The reactor was also operable with n-hexane, but the operational stability of the immobilized enzyme in n-hexane was only half of that in isooctane. Our results indicate that various enzyme carrier having hydrophilic or amphiphilic properties could be used for two-phase continuous reaction in packed-bed column, reactor without any surfactant supply or prior dispersion of the two immiscible phases. (c) 1992 John Wiley & Sons, Inc.     

A comparison of lipase-catalyzed ester hydrolysis in reverse micelles, organic solvents, and biphasic systems

The performance of lipases from Candida rugosa and wheat germ have been investigated in three reaction media using three acetate hydrolyses as model reactions (ethyl acetate, allyl acetate, and prenyl acetate). The effect of substrate properties and water content were studied for each system (organic solvent, biphasic system, and reverse micelles). Not unexpectedly, the effect of water content is distinct for each system, and the optimal water content for enzyme activity is not always the same as that for productivity. A theoretical model has been used to simulate and predict enzyme performance in reverse micelles, and a proposed partitioning model for biphasic systems agrees well with experimental results. While the highest activities observed were in the micellar system, productivity in microemulsions is limited by low enzyme concentrations. Biphasic systems, however, support relatively good activity and productivity. The addition of water to dry organic solvents, combined with the dispersion of lyophilized enzyme powders in the solvent, resulted in significant enzyme aggregation, which not surprisingly limits the applicability of the "anhydrous" enzyme suspension approach. (c) 1995 John Wiley & Sons, Inc.     

Lipase-catalyzed transamidation of non-activated amides in organic solvent

A novel biocatalytic reaction of transamidation of non-activated amides with amines is reported. Among 45 different lipolytic and proteolytic enzymes tested, only the lipase from Candida antarcticawas able to catalyze this reaction. The reaction proceeded with up to ca. 80% conversion in anhydrous methyl tert-butyl ether and worked with both N-substituted and unsubstituted amides. The biocatalytic transamidation is an equilibrium process and, therefore, higher conversions to the desired amide were achieved by using increased concentrations of the amine nucleophile.     

Synthesis of phosphatidylcholine with defined fatty acid in the sn-1 position by lipase-catalyzed esterification and transesterification reaction

The incorporation of caproic acid in the sn-1 position of phosphatidylcholine (PC) catalyzed by lipase from Rhizopus oryzae was investigated in a water activity-controlled organic medium. The reaction was carried out either as esterification or transesterification. A comparison between these two reaction modes was made with regard to product yield, product purity, reaction time, and byproduct formation as a consequence of acyl migration. The yield in the esterification and transesterification reaction was the same under identical conditions. The highest yield (78%) was obtained at a water activity (a(w)) of 0.11 and a caproic acid concentration of 0.8 M. The reaction time was shorter in the esterification reaction than in the transesterification reaction. The difference in reaction time was especially pronounced at low water activities and high fatty acid concentrations. The loss in yield due to acyl migration and consequent enzymatic side reactions was around 16% under a wide range of conditions. The incorporation of a fatty acid in the sn-1 position of PC proved to be thermodynamically much more favorable than the incorporation of a fatty acid in the sn-2 position.     

Lipase-catalyzed methanolysis of palm oil in presence and absence of organic solvent for production of biodiesel

Enzymatic production of methyl esters (biodiesel) by methanolysis of palm oil in presence and absence of organic solvent was investigated using Candida antarctica lipase immobilized on acrylic resin as a biocatalyst. Although, at least molar equivalent of methanol (methanol-palm oil ratio 3:1) is required for the complete conversion of palm oil to methyl esters, lipase catalyzed methanolysis of palm oil in absence of organic solvent was poisoned by adding more than 1/3 molar equivalent of methanol. The use of polar organic solvents prevented the lipase to be poisoned in methanolysis with a molar equivalent of methanol, and tetrahydrofuran (THF) was found to be the most effective. The presence of water in methanolysis of palm oil both in presence and absence of THF inhibited the reaction rate but this inhibition was considerably low in THF containing system. The palm oil-lipase (w/w) ratio significantly influenced the activity of lipase and the optimal ratio in presence and absence of THF was 100 and 50, respectively.     

Application of solvent engineering to optimize lipase-catalyzed 1,3-diglyacylcerols by mixture response surface methodology

1,3-Diacylglycerol has been introduced in Japan as a cooking oil under the trade name of Econa to reduce body fat accumulation. Solvent engineering was applied to determine the optimum solvent mixtures for the lipase-catalyzed synthesis of 1,3-DAG by mixture response surface methodology. n-Hexane was required to maintain the lipase activity and the product selectivity could be adjusted by changing the hydrophobicity of reaction medium. The optimum yield (40%) of 1,3-DAG synthesis was obtained with n-hexane/octane (1:1, v/v).     

Papain kinetics in the presence of a water-miscible organic solvent

The effects of various concentrations of a water-miscible organic solvent [a 7:3 (v/v) mixture of N, N dimethylformamide and dimethylsulfoxide] on the kinetics of papain have been investigated. The parameters k(cat) and K(m) for the amidase and esterase activity of papain using N-alpha-benzoyl-DL-arginine-p-nitroanilide (BAPNA) and N-alpha-benzoyl-L-arginine ethyl ester (BAEE) as substrates were determined. For both types of activity, k(cat) initially increased (up to about 15% solvent), and then decreased with increasing concentrations of organic solvent. In contrast, K(m) increased sharply with the organic solvent concentration. Active site titration at 0 and 50% solvent indicated no change in the amount of active enzyme. Fluorometric measurements of the emission spectrum of papain did not indicate any major conformational changes with increasing concentrations of organic solvent.     

Preparation of the gemini detergent-lipase complexes and their high enzymatic activities in the transesterifications in homogeneous organic solvents

Lipase and newly synthesized gemini-type detergent were mixed in an aqueous phosphate buffer solution and lyophilized. Due to complex formation between the substances it was possible to dissolve or at least finely disperse these preparations in organic media. The lipase-detergent complexes were used to catalyse the irreversible transesterfication of 6-methyl-5-hepten-2-ol (sulcatol) or 2,2-dimethyl-1,3-dioxolane-4-methanol (solketal) with vinyl or isopropenyl carboxylate in organic solvents. The complexes were considerably more active than enzyme powder or the complexes prepared with conventional synthesized detergents in organic media. © Rapid Science Ltd. 1998     

Thermodynamic parameters monitoring the equilibrium shift of enzyme-catalyzed hydrolysis/synthesis reactions in favor of synthesis in mixtures of water and organic solvent

The main strategy developed to shift the equilibrium state of a hydrolase-catalyzed hydrolysis/synthesis reaction consists in reducing water activity by addition of organic solvents in the reaction medium. We have used several mixtures of water and 1,4-butanediol, ranging from pure water to pure 1,4-butanediol, to study the hydrolysis/synthesis reaction of the N-Cbz-L-tryptophanyl-glycineamide dipeptide, catalyzed by alpha-chymotrypsin. In the presence of 1,4-butanediol, alpha-chymotrypsin also catalyzed the esterification reaction between this diol and N-Cbz-L-tryptophan; this ester hydrolysis/synthesis reaction has thus also been examined. The dipeptide and ester equilibrium concentrations increase when the water content of the reaction medium is decreased. Using our experimental data, we have determined the equilibrium constants of the hydrolysis/synthesis equilibria involving the nonionized forms of the protected amino acids, the estimated values of which are Ksp = 8 10(5) for the dipeptide and Kse = 78 for the ester respectively. They are true thermodynamic equilibrium constants, each related to a single, well-defined reaction equilibrium and with water activity being taken into account. If an organic solvent is added to the reaction medium these equilibria can be shifted towards synthesis by decreasing the water activity but also by modifying the ionization/neutralization equilibrium constant of the ionizable groups. These two effects depend both on the water content and on the nature of the organic solvent used, and, in particular, on its dielectric constant. Because of the importance of this parameter in our study, we discuss using it as an indicator to select an appropriate organic solvent to perform an enzyme-catalyzed synthesis.     

Simple screening method for lipase for transesterification in organic solvent

We investigated lipase-catalyzed hydrolysis in water and dioxane—water with a simple colorimetric method. We screened 24 lipases for the ability to hydrolyze p-nitrophenyl esters as chromogenic substrates. Their hydrolytic activities were varied by adding dioxane. Most of the lipases showed high activity in hydrolysis in water, but some showed activity in 50% dioxane—water several tens times higher than those in water. Moreover, several lipases with hydrolytic abilities in 50% dioxane—water also catalyzed the transesterification of p-nitrophenol using fatty acid vinyl esters. We found it possible that a useful lipase for transesterification can be selected by measuring the hydrolysis activity of p-nitrophenyl ester in 50% dioxane—water.     

Improving lipase-catalyzed enantioselective ammonolysis of phenylglycine methyl ester in organic solvent by in situ racemization

Lipase-catalyzed enantioselective ammonolysis of phenylglycine methyl ester was processed by in situ racemization with ammonium carbamate as the acyl acceptor. Using 1 mM benzaldehyde or 0.6 mM chloropyridoxal as the racemizing catalyst, 80% substrate conversion with an enantiomeric excess of the product of 95% were achieved at 20 °C after 7 h reaction.     

Reactivation of Horseradish peroxidase in organic solvent using extraction

A novel extraction method was developed aiming at increasing the stability of enzymes in organic solvent media. Horseradish peroxidase (HRP), inactivated in a tetrahydrofuran (THF)/water (1:1, v/v), regained and maintained its activity when HRP was extracted by adding a THF/benzene mixture to the original solution. However, the HRP activity was drastically lowered in the enzyme-free blank solution that had been formed by employing the same extraction procedure. As a result, the reactivation after the extraction is believed to depend on enzyme history, and might be arisen from an irreversible structural change of the enzyme.     

Computer-aided real-time estimation of reaction conversion for lipase-catalyzed esterification in solvent-free systems

Real-time conversion estimation through macroscopic balancing was investigated for enzymatic esterification reactions in a solvent-free system. In principle, the conversion of ester synthesis can be determined from the amount of water produced by the reaction because water is formed as a by-product in the same molar ratio as the product. In this study, we show that the water production rate, and thereby the reaction conversion, can be estimated on-line from measurements of the relative humidity of the inlet and outlet air and the material balances of water in the system. In order to test the performance of the real-time conversion estimation method, the lipase-catalyzed esterification reaction of n-capric acid and n-decyl alcohol in solvent-free media was conducted while controlling the water activity at various values. When the reaction conversions estimated on-line were compared with those analyzed off-line by gas chromatography, good agreement was obtained: the average mean absolute error was +/- 2.4% of the reaction conversion despite the simplicity of the method. The on-line estimation method presented here requires no expensive or complicated analytical instruments and no sampling of reaction medium. It can be used for monitoring nonaqueous enzymatic reactions where water is produced or consumed during reaction.     

腐生葡萄球菌M36耐有机溶剂脂肪酶基因的克隆与原核表达

脂肪酶是重要的工业用酶,在食品加工、生物柴油的合成等领域具有广泛的应用。但是在应用中有机溶剂对脂肪酶具有一定的毒性,因此获得耐有机溶剂的脂肪酶基因并实现高效表达是脂肪酶规模化应用的前提。本研究应用PCR技术首次从耐有机溶剂脂肪酶产生菌腐生葡萄球菌M36基因组DNA中扩增得到脂肪酶Ⅲ基因lip3(GenBank AccessionNo.FJ979867),其编码区长度为741bp,编码247个氨基酸,推测蛋白分子量大小为31.6kD。它与腐生葡萄球菌lip3推测的基因(GenBank AccessionNo.AP008934)只有83%的同源性。将该基因与大肠杆菌表达载体pET-DsbA连接,转化大肠杆菌EscherichiacoliBL21(DE3)获得重组菌株BL21(DE3)/pET-DsbA-lip3,在pH8、25oC条件下,OD600为1.0时用0.4mmol/LIPTG诱导12h酶活达到25.8U/mL。重组酶在甲醇、正己烷、异辛烷、正庚烷等有机溶剂中具有较好的耐性。lip3基因的克隆及在大肠杆菌中有效表达的研究为进一步进行基因工程改造和脂肪酶应用奠定了基础。     

Lipase-catalyzed esterification of 2-(4-substituted phenoxy)propionic acids in organic solvents: substituent effect controlling enantioselectivity toward racemic acids

The enantioselectivity for lipase-catalyzed esterifications of 2-(4-substituted phenoxy)propionic acids in organic solvents was found to be mainly controlled by both size (steric) and electronic effects of substituents: H, F, Cl, CF₃ and CH₃. For the similar substituents in size, CF₃ and CH₃, however, their electronic effects play an important role in controlling the enantioselectivity. A model for the enantiorecognition is proposed by the discussion based on the value of the Michaelis constant obtained for the enantiomers.     

A new method for improving the enantioselectivity of lipase-catalyzed hydrolysis in organic solvent containing a small amount of water in the presence of metal ions

The hydrolysis of racemic butyl 2-(4-substituted phenoxy)propionates having various substituents catalyzed by lipase MY from Candida rugosa was achieved in di-isopropyl ether containing 0.75% (v/v) of 2.4 M LiCl or 1.2 M MgCl₂ aqueous solution. Water molecules hydrated to the metal ion in isopropyl ether acted as a nucleophile to cause the hydrolysis of these esters as with water alone. Metal ions used significantly enhanced their enantioselectivities by 100-fold or above, as compared with the ordinary reaction media.     

Lipase-catalyzed condensation of p-methoxyphenethyl alcohol and carboxylic acids with different steric and electrical properties in acetonitrile

The substrate selectivity of Candida antarctica lipase for various carboxylic acids was systematically investigated for their condensation with p-methoxyphenethyl alcohol in acetonitrile. The electron density of a carboxylic carbon and the projection area of an acid molecule were numerical indicators for evaluating the substrate selectivity. Both the electron density and projection area had an influence on the V/K _m value, while only the projection area affected the K _m value. The presence of conjugation with a carboxyl group in an acid and a branched structure in the non-carboxylic region independently lowered the V/K _m value by an order of 1.