Surfactant-Modified lipase for the catalysis of the interesterification of triglycerides and fatty acids

The lipase-catalyzed intresterification of triglycerides and fatty acids in n-hexane was studied. Initially, lipase Saiken was modified with a surfactant of sorbitan esters so that its dispersibility in hydrophobic organic media was improved. The surfactant-modified lipase formed in the modification process carried out in a buffer solution has 1,3-positional specificity and predominantly catalyzed the interesterification reaction in a microaqueous n-hexane system. The modification technique converted inactive lipases to very active biocatalysts for the interesterification of triglycerides and fatty acids. The pH and the weight ratio of surfactant to enzyme used during the lipase modification process have shown significant effects in determining the recoveries of the protein and enzyme activity from the buffer solution, the protein content of the modified lipase complex after being freeze dried, and the interesterification activity of the complex. The water content in the reaction solution has strongly influenced the enzyme activity as well as the distribution of the products. (c) 1995 John Wiley & Sons, Inc.     

Esterification reactions of lipase in reverse micelles

The activities of lipase from Candida cylindracea and Rhizopus delemar have been investigated in water/AOT/iso-octane reverse micellar media through the use of two esterification reactions: fatty acid-alcohol esterification and glyceride synthesis. Such media promotes the occurrence of these two lipase-catalyzed reactions due to its low water content. The effect of various parameters on the activity of lipase from C. cylindracea in reverse micelles was determined and compared to results where alternate media were employed. It was observed that the structure of the media, as dictated by the type and concentration of the substrates and products and by the water/AOT ratio, w(0), had a strong impact on enzyme activity. Strong deactivation of both typase types occurred in reverse micelles, especially in the absence of substrates and for w(0) values greater than 3.0. Glyceride synthesis was realized with lipase from R. delemar, but not with that from C. cylindracea; the temperature and concentration of substrates and water strongly dictated the reaction rate and the percent conversion.     

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.     

Characteristics of Lipase Catalysis During Ester Synthesis in Reversed Micellar Systems

The ability of lipase from Candida cylindracea to catalyze ester synthesis from a long chain fatty acid (palmitic acid) and alcohols of varying chain length, is examined. The enzyme is located in the minimal-water environment of reversed micelles. Lipase activity is a strong function of the mode of encapsulation. Direct solid lipase addition to reversed micelles leads to encapsulation in an inactive state unless the enzyme is contacted with the acyl substrate. The alcohol inhibits activity, with low molecular weight alcohols tending to denature the enzyme. Implications to reversed micelle based biocatalyst preparation are briefly discussed.     

Enantioselective synthesis of ibuprofen esters in AOT/isooctane microemulsions by Candida cylindracea lipase

The enantioselective esterification of racemic ibuprofen, catalyzed by a Candida cylindracea lipase, was studied in a water-in-oil microemulsion (AOT/isooctane). By using n-propanol as the alcohol, an optimal W(0) ([H(2)O]/[AOT] ratio) of 12 was found for the synthesis of n-propyl-ibuprofenate at room temperature. The lipase showed high preference for the S(+)-enantiomer of ibuprofen, which was esterified to the corresponding S(+)-ibuprofen ester. The R(-)-ibuprofen remained unesterified in the microemulsion. The calculated enantioselectivity value (E) for S-ibuprofen ester was greater than 150 (conversion 0.32). The enzyme activities of n-alcohols with different chain lengths (3-12) were compared, and it appeared that short- (propanol and butanol) and long-chained (decanol and dodecanol) alcohols were better substrates than the intermediate ones (pentanol, hexanol, and octanol). However, unlike secondary and tertiary alcohols, all of the tested primary alcohols were substrates for the lipase. The reversible reaction (i.e., the hydrolysis of racemic ibuprofen ester in the microemulsion) was also carried out enantioselectively by the enzyme. Only the S form of the ester was hydrolyzed to the corresponding S-ibuprofen. The reaction yield was, however, only about 4% after 10 days of reaction. The corresponding yield for the esterification of ibuprofen was about 35% (10 days). The high enantioselectivity displayed by the lipase in the microemulsion system was seen neither in a similar esterification reaction in a pure organic solvent system (isooctane) nor in the hydrolysis reaction in an aqueous system (buffer). The E value for S-ibuprofen ester in the isooctane system was 3.0 (conversion 0.41), and only 1.3 for S-ibuprofen in the hydrolysis reaction (conversion 0.32). The differences in enantioselectivity for the lipase in various systems are likely due to interfacial phenomena. In the microemulsion system, the water in which the enzyme is dissolved is separated from the solvent by a layer of surfactant molecules, thus creating an interface with a relatively large area. Such interfaces are not present in the pure organic solvent systems (no surfactant) nor in aqueous systems. (c) 1993 John Wiley & Sons, Inc.     

Production of high-oleic acid tallow fractions using lipase-catalyzed directed interesterification, using both batch and continuous processing

Immobilized lipases were used to catalyze batch-directed interesterification of tallow, resulting in oleins containing significantly higher levels of unsaturated fatty acids than obtained by fractionation without lipase. After 14 days, a reaction catalyzed by 2% Novozym 435 yielded 57% olein unsaturation, compared with 45% in a no-enzyme control. Free fatty acid levels increased to 2-3% during reactions. Incubation of the enzyme in multiple batches of melted fat caused a gradual loss of interesterification activity, apparently due to progressive dehydration. The activity could be restored by addition of water to the reaction medium. Immobilized lipase was also used to catalyze directed interesterification in a continuous flow reactor. Melted tallow was circulated through a packed bed enzyme reactor and a separate crystallization vessel. The temperatures of the two parts of the apparatus were controlled separately to allow crystallization to occur separately from interesterification. Operation of the reactor with conventionally dry, prefractionated tallow allowed the formation of an olein consisting of up to 60% unsaturated fatty acids. The greatest changes in olein fatty acid composition were achieved when the fractionation temperature was kept constant at a value that promoted selective crystallization of trisaturated triglycerides that were continuously produced by enzymic interesterification. The enzyme could be reused without apparent loss of activity, and its activity was apparently enhanced by preincubation in melted tallow for up to several days. Control of both the water activity of the enzyme and tallow feedstock and of the absorption of atmospheric water vapor were required to maintain enzyme activity, during multiple reuse and minimize free fatty acid formation. This method may form the basis for a process to produce highly mono-unsaturated tallow fractions for use in food applications (e.g. frying) where a "healthy" low saturated fat product is required.     

Resolution of d,l-menthol by interesterification with triacetin using the free and immobilized lipase of Candida cylindracea

Summary Interesterification in isooctane with triacetin as an acyl donor was found to be a new and effective method of racemic resolution of d,l-menthol, when using the free and immobilized lipase of Candida cylindracea. No water was produced by this highly stereoselective type of reaction in contrast to ester synthesis with acetic acid as an acyl donor. Even with diacetin no possible back reaction occurred and the enzyme was easily separated from the reaction solution as opposed to ester hydrolysis in aqueous systems. Inhibition of interesterification was caused by increasing concentrations of the acyl donor triacetin by more than 10 mmol·l^-1 on the one hand, and especially by diacetin on the other hand. The reaction product menthyl acetate had no influence. By adding water the interesterification activity of the lipase was reduced significantly. An alteration of the acyl donor triacetin to longerchained triglycerides caused changes in higher specific activities but poor enantioselectivities of the products, as in the case of ester synthesis starting from longer-chained organic acids.Dedicated to Prof. Dr. Fritz Wagner on the occasion of his 60th birthday     

Pseudomonas cepacia lipase: Esterification reactions in AOT microemulsion systems

Summary The activity of purifiedPseudomonas cepacia lipase has been investigated in esterification reactions of various aliphatic alcohols with natural fatty acids. The reactions were carried out in microemulsions formed in isooctane by bis(2ethylhexyl)sulfosuccinate sodium salt (AOT). The optima pH, T and water content (w_o) for the enzyme activity in this type of microemulsions have been determined. Studies on the effect of various fatty acids and alcohols on the enzyme specificity have shown a preference of this lipase for palmitic and caprylic acid as well as for propanol, while reactions involving cyclic alcohols can not be catalyzed at all. The differences on the behavior of this lipase as compared to other lipases studied in microemulsion systems as well as in other systems are discussed.     

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…     

Lipase activity in vesicular systems: characterization of candida cylindracea lipase and its activity in polymerizable dialkylammonium surfactant vesicles

Lipase from Candida cylindracea (CCL) was incorporated into polymerizable positively charged dialkylammonium bromide surfactant vesicles. The enzyme was incorporated by the use of the dehydration-rehydration method or by incubation. In the latter case, trapping efficiencies of up to 100% could be obtained. Activities of free and vesicle-incorporated CCL were tested for three triglycerides: triacetin, tributyrin, and tricaprylin. Enzyme activity was lowest in homogeneous mixtures (triacetin and small concentrations of tributyrin) and highest in heterogeneous mixtures (tricaprylin and high concentrations of tributyrin). Entrapment in vesicular systems is advantageous, especially in homogeneous reaction mixtures and in the case of the production of insoluble fatty acid (caproate), because inhibition by the acid can be suppressed. The influence of several surface-active additives, including vesicles, on the activity of lipase in triglyceride assays was tested. Vesicles have a positive influence on the activity, whereas other positively charged additives act as inhibitors. In the case of tricaprylin assays, the positively charged additives increase the activity. Finally, tryptic digestion for free and incorporated CCL were compared. Free CCL is readily inactivated, whereas incorporated enzyme is protected from proteolytic degradation. (c) 1993 John Wiley & Sons, Inc.     

Characteristics of lipase-catalyzed hydrolysis of olive oil in AOT-isooctane reversed micelles

Candida rugosa lipase solubilized in organic solvents in the presence of both surfactant and water could catalyze the hydrolysis of triglycerides, and kinetic analysis of the lipase-catalyzed reaction was found to be possible in this system. Among eight organic solvents tested, isooctane was most effective for the hydrolysis of olive oil in reversed micelles. Temperature effect, pH profile, K(m,app) and V(max,app) were determined. Among various chemical compounds, Cu(2+), Hg(2+), and Fe(3+) inhibited lipase severely. But the enzyme activity was restorable partially by adding histidine or glycine to the system containing these metal ions. The enzyme activity was dependent on R (molar ratio of water to surfactant) and maximum activity was obtained at R = 10.5. Upon addition of glycerol to the reversed micelles, lipase activity was affected in a different fashion depending on the R values. Stability of the lipase in reversed micelles was also dependent on R, and it was most stable at R = 5.5.     

Esterification reactions catalyzed by Chromobacterium viscosum lipase in CTAB-based microemulsion systems

Chromobacterium viscosum (CV) lipase solubilized in water-in-oil (w/o) microemulsions based on the cationic surfactant hexadecyltrimethylammonium bromide (CTAB) have been used for multigram-scale ester synthesis, including the kinetic resolution of a secondary alcohol. The stability of CV lipase in all the CTAB microemulsions studied was excellent and was superior to that observed in aqueous buffer at the same pH and temperature. Kinetic studies were performed using the synthesis of ethylhexadecanoate as a model reaction. Under pseudo-first-order conditions, the synthesis rates were linearlydependent on the enzyme and fatty acid concentrations and the R dependence shows the characteristic bell-shaped curve (where R = [H(2)O]/[surfactant]). The dependence of enzyme activity toward octyldecanoate synthesis on the pH of the dispersed buffer phase is in marked contrast to that observed for the pH dependence of CV lipase toward p-nitrophenylbutyrate hydrolysis. In the former case, the pH-activity profile is approximately sigmoidal, which may reflect the ionization state of the fatty acid substrate. In the latter case, the pH dependence is minimal at both R = 10 and R = 50, suggesting the enzyme does not experience a changed pH environment. Inclusion of a pH-sensitive probe molecule into those incubations containing fatty acid clearly demonstrates that the probe molecule experiences a changed environment consistent with that expected for the selected buffer. An in situ Fourier transform nuclear magnetic resonance (FT-NMR) assay has been developed which allows continuous monitoring of the esterification reactions, thereby providing an additional means of determining initial rates. The method may be of general value for lipase assays in microemulsions since it may provide, at the same time, information regarding enzyme regioselectivity. (c) 1995 John Wiley & Sons, Inc.     

Esterification of phenolic acids catalyzed by lipases immobilized in organogels

Lipases from Rhizomucor miehei and Candida antarctica B were immobilized in hydroxypropylmethyl cellulose organogels based on surfactant-free microemulsions consisting of n-hexane, 1-propanol and water. Both lipases kept their catalytic activity, catalyzing the esterification reactions of various phenolic acids including cinnamic acid derivatives. High reaction rates and yields (up to 94%) were obtained when lipase from C. antarctica was used. Kinetic studies have been performed and apparent kinetic constants were determined showing that ester synthesis catalyzed by immobilized lipases occurs via the Michaelis–Menten mechanism.     

Lipase catalysed synthesis of optically enriched alpha-haloamides

An efficient lipase catalysed synthesis of optically enriched alpha-halogenated amides with concomitant optical enrichment of the starting alpha-haloesters is described. Candida antarctica lipase (CAL) was found to be a better catalyst over porcine pancreatic lipase (PPL) and Candida cylindracea lipase (CCL). The effect of different organic solvents was also studied.     

Modification of the Microenvironment of Enzymes in Organic Solvents. Substitution of Water by Polar Solvents

Enzyme catalysis in water-immiscible organic solvents is strongly influenced by the amount of water present in the reaction mixture. Effects of substitution of part of the water by other polar solvents were studied. In an alcoholysis reaction catalyzed by chymotrypsin deposited on celite, it was possible to exchange half of the water by formamide, ethylene glycol or dimethyl sulfoxide with often increased initial reaction rate. Furthermore, these substitutions caused the suppression of the competing hydrolysis reaction. However, formamide caused enzyme inactivation, and ethylene glycol participated as a reactant in the alcoholysis to some extent, hence dimethyl sulfoxide was considered the best water substitute among the solvents tested. These effects were noted for chymotrypsin catalyzed alcoholysis in several water immiscible solvents and also for interesterification reactions catalyzed by Candida cylindracea lipase on celite. In the latter case a change in the stereoselectivity was observed. At a low water content a high stereoselectivity was observed; when the amount of polar solvent was increased, either by doubling the water content or adding an equal amount of DMSO, the stereoselectivity decreased.     

Enzymatic transesterifications of carbonates in water-restricted environments

We investigated the ability of several hydrolases to catalyze reactions with an abiotic water-insoluble substrate, carbonic acid diphenyl ester, also known as diphenyl carbonate (DPC). In single-phase water/organic systems, turnover numbers (TN) of greater than 2 x 10(4) min(-1)have been achieved for the hydrolysis of DPC. The K(m) values for the hydrolytic reaction were measured to be 200muM and 330muM for Candida cylindracea lipase and Porcine liver esterase, respectively. In addition to hydrolysis, we observed transesterification of carbonates with a wide variety of alcohol and phenol species. Transesterifications of DPC with bifunctional alcohols resulted in the synthesis of polycarbonates. We investigated the stability and transesterification activity of these enzymes in several water-restricted environments to limit competing hydrolysis reactions. We find that, with the removal of water, hydrolysis is reduced more than four orders of magnitude while transesterification is diminished only 10-fold (turnover numbers of 600 min(-1) in water-miscible systems to 60 min(-1) in water-restricted environments with pure Candida lipase). Stability of the Candida lipase in these water-restricted environments (half-life of longer than 3 days) is much greater than in water/organic single phase systems (5 h in 20% methanol). In addition, the Candida lipase displayed enantiomeric selectivity in transesterifications of DPC with racemic 2-butanol (greater than 80% ee).     

Modulation of lipase hydrolysis and synthesis reactions using carbohydrates.

A novel method for modulation of lipase hydrolysis and synthesis lipase was investigated by using carbohydrates in the microenvironment of the Candida rugosa enzyme. The influence of the addition of different sugars to the previously dialysed enzyme was tested on the two reactions. Rates of hydrolysis were lowered by using dialysed enzyme but were increased after sugar addition, regardless of the identity of the added sugar. In contrast, synthesis reaction rates depended on the nature of the carbohydrate. Rates were increased by adding lactose, which is not a water activity depressor, but were lowered by adding fructose, glucose, sucrose or sorbitol, which are all water activity depressors.     

Improved triglyceride transesterification by circular permuted Candida antarctica lipase B

Lipases represent a versatile class of biocatalysts with numerous potential applications in industry including the production of biodiesel via enzyme‐catalyzed transesterification. In this article, we have investigated the performance of cp283, a variant of Candida antarctica lipase B (CALB) engineered by circular permutation, with a series of esters, as well as pure and complex triglycerides. In comparison with wild‐type CALB, the permutated enzyme showed consistently higher catalytic activity (2.6‐ to 9‐fold) for trans and interesterification of the different substrates with 1‐butanol and ethyl acetate as acyl acceptors. Differences in the observed rates for wild‐type CALB and cp283 are believe to be related to changes in the rate‐determining step of the catalytic cycle as a result of circular permutation. Biotechnol. Bioeng. 2010;105: 44–50. © 2009 Wiley Periodicals, Inc.     

Immobilized Pseudomonas cepacia lipase for biodiesel fuel production from soybean oil

Enzymatic transesterification of soybean oil with methanol and ethanol was studied. Of the nine lipases that were tested in the initial screening, lipase PS from Pseudomonas cepacia resulted in the highest yield of alkyl esters. Lipase from Pseudomonas cepacia was further investigated in immobilized form within a chemically inert, hydrophobic sol-gel support. The gel-entrapped lipase was prepared by polycondensation of hydrolyzed tetramethoxysilane and iso-butyltrimethoxysilane. Using the immobilized lipase PS, the effects of water and alcohol concentration, enzyme loading, enzyme thermal stability, and temperature in the transesterification reaction were investigated. The optimal conditions for processing 10 g of soybean oil were: 35 degrees C, 1:7.5 oil/methanol molar ratio, 0.5 g water and 475 mg lipase for the reactions with methanol, and 35 degrees C, 1:15.2 oil/ethanol molar ratio, 0.3 g water, 475 mg lipase for the reactions with ethanol. Subject to the optimal conditions, methyl and ethyl esters formation of 67 and 65 mol% in 1h of reaction were obtained for the immobilized enzyme reactions. Upon the reaction with the immobilized lipase, the triglycerides reached negligible levels after the first 30 min of the reaction and the immobilized lipase was consistently more active than the free enzyme. The immobilized lipase also proved to be stable and lost little activity when was subjected to repeated uses.     

Restoration of Rice Husk-Adsorbed Lipase Activity after Rehydration

Hydrolytic and esterifying activities of lipase from Candida cylindracea adsorbed on rice husks were lost by dehydration using molecular sieve pellets and P₂O₅which removed 90-97% of the water after 9 days. However, only the esterifying activity of the enzyme was restored by gradual water transfer via the organic phase to the dried enzyme either by direct water addition or by using salt hydrates as water donors.