Synthesis of fatty acid esters by a recombinant cutinase in reversed micelles

Fusarium solani pisi recombinant cutinase, solubilized in AOT/isooctane-reversed micelles, was used to catalyze the esterification of fatty acids with aliphatic alcohols. Some relevant parameters for the enzyme activity such as pH, W(o) (water/surfactant molar ratio), temperature, and substrate concentration were optimized. Maximal specific activity was obtained for hexanol. The cutinase showed selectivity for short-chain fatty acids. The stability of the microencapsulated cutinase was investigated at various concentrations of water and different values of pH. Oleic acid had a negative effect on the cutinase stability, while hexanol proved to be a strong stabilizer increasing the half-life of the enzyme about 45 times. (c) 1993 John Wiley & Sons, Inc.     

Two-Step biocatalytic conversion of an ester to an aldehyde in reverse micelles

Lipases from Candida cyclindracea (L-1754) and wheat germ (L-3001) have been used to hydrolyze esters to their corresponding alcohols and acids in reverse micelles. Alcohol dehydrogenase from baker's yeast (YADH) was subsequently used to reduce the alcohol products to aldehydes. Cofactor recycling in the redox reaction was achieved using a sacrificial cosubstrate, as described previously. Four surfactants (sodium dioctylsulfosuccinate, Nonidet P-40 with Triton X-35, polyoxyethylene, 10-cetyl-ether, polyoxyethylene sorbitan trioleate) were employed to determine the effect of amphiphile on ester hydrolysis and redox reaction rates separately. The effect of type of organic solvent, W(0) [(water]/[surfactant)], and substrate concentration on separte enzyme activity were also investigated. A brief investigation of a single phase, two-step reaction catalyzed by the combination of lipase and YADH in reverse micelles is also reported. The activities of the enzymes are significantly different when used together instead of independently. (c) 1994 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.     

Tyrosinase activity in reversed micelles

The hydroxylase and oxidase activities of mushroom tyrosinase were studied in both sodium di-2-ethylhexylsulfosuccinate (AOT)/isooctane and cetyltrimethylammonium bromide (CTAB)/hexane/chloroform reversed micelles. The enzyme presented its highest activity when the water to surfactant molar ratio (W ₀) was 20 for both systems. When entrapped in the AOT reversed micelles, the enzyme activity decreased with the increase in AOT concentration at a constant W ₀, and the enzyme not only presented a higher reaction rate related to its oxidase activity but also a shorter lag period related to its hydroxylase activity. The relation between water activity and W ₀ revealed that enzyme activity in reversed micelles was more related to the size of the micelles which was determined by W ₀ and less to the water activity. Tyrosinase in CTAB reversed micelles showed potential for the analysis of o-diphenols.     

Solubilizing water involved in protein extraction using reversed micelles

The extraction of protein using reversed micelles was investigated in relation to the amount of solubilizing water in the reversed micellar organic phase. The minimal concentration of amphiphilic molecule di-2-ethylhexyl sodium sulfosuccinate (C(20)H(37)O(7)Na) (AOT) required for 100% cytochrome c extraction was recognized. This critical AOT concentration increased with protein concentration in the aqueous phase. On this minimal AOT condition, the molar ratio of solubilizing water to extracted protein was found to be a constant of 3500 under C(KCI) = 1.0 x 10(2) mol . m(-3) in this system. This ratio means the hydrophillic surroundings required for extracting one protein molecule into the micellar organic phase under the suitable pH and salt concentration for the forward extraction. In this regard, AOT molecules seemed to take the part of water solubilizing agent in the reversed micellar extraction. This role of AOT is important to extract protein under the suitable pH and salt concentration. The amount of solubilizing water in the protein-containing system was larger than in the protein-free system. This difference shows that the water molecules accompany the extracted protein into the reversed micellar organic phase at constant ratio 2200 under C(KCI) = 1.0 x 10(2) mol . m(-3), i.e., accompanying water molecules per one extracted protein. The minimal AOT concentration increased with ionic strength. On this minimal AOT condition, the molar ratio of solubilizing water to extracted protein also increased with ionic strength, so that in higher ionic strength, more solubilizing water was required. Then more AOT was required to provide the hydrophillic surroundings for protein. The pH affected the minimal AOT concentration required for 100% protein extraction.     

Mechanisms of amino acid partitioning in cationic reversed micelles

The aim of this work is to discuss the mechanisms involved in amino acidsolubilization in cationic reversed micelles. A simple mechanism was assumedin which the amino acid solubilization is mediated by an ion-exchangeprocess between the amino acid and the surfactant counter ion neglecting theeffect of the reversed micellar structure. Based on this mechanism a simplemodel to predict equilibrium was developed and applied to the solubilizationof amino acids with different structures. It was found that solubilizationof hydrophilic and slightly hydrophobic amino acids can be described by anion-exchange mechanism and the amino acid equilibrium concentration can bedetermined for different experimental conditions using this model. However,solubilization of hydrophobic amino acids can not be described by a simpleion-exchange model. In this case hydrophobic contributions play an importantrole in amino acid solubilization and must be considered in the overallsolubilization process. This hydrophobic contribution was evaluated bydetermination of an interfacial partition coefficient. The overall aminoacid extraction was determined using distribution coefficients of all theamino acid forms and considering their dependence on ionic strength.     

EPR characterizations of alpha-chymotrypsin active site dynamics in reversed micelles at enhanced gas pressures and after subjection to clathrate formation conditions

Electron paramagnetic resonance spectroscopy is used to characterize the active site dynamics of alpha-chymotrypsin solubilized in reversed micelles. Of particular interest is the behavior of the enzyme when the micellar system is subjected to enhanced gas pressures and low temperatures. At specific thermodynamic conditions, clathrate hydrates from from the intramicellar water, reducing the micelle size and water content. Also, beyond a critical pressure, micellar instbility results. The EPR spectra under these conditions indicate that the rotational correlation times increase appreciably only when the water-to-surfactant molar ratio, W(0), is reduced to values lower than 10. The EPR characterization also reveals a remarkable resilience of the enzyme when subjected to pressure-induced changes; when returned to ambient conditions, activity and active site dynamics are fully restored. (c) 1994 John Wiley & Sons, Inc.     

Amidase encapsulated in TTAB reversed micelles for the study of transamidation reactions

Amidase, an amide hydrolase enzyme (E.C.3.5.1.4) with acyl transferase activity, was encapsulated in a reversed micellar system composed of the cationic surfactant tetradecyltrimethyl ammonium bromide (TTAB) in heptane/octanol (80/20%) and phosphate buffer at w ₀ 11. The reaction used to study the effect of the reversed micellar system on the enzyme behaviour was a transamidation reaction. The effect of surfactant concentration, buffer molarity and pH on the enzyme kinetics was evaluated. Both initial velocities and product yield were measured. The results indicated that a high initial velocity of hydroxamic acid synthesis and also the highest yield (98%) were obtained using the lowest pH value. The effect of TTAB concentration was dependent on the buffer molarity used. The effect of buffer molarity on reversed micelle dimensions was analysed by light scattering. These results showed that the buffer molarity had a strong influence on the reversed micelle radius that correlated with enzyme activity.     

Amidase encapsulated in TTAB reversed micelles for the study of transamidation reactions

Amidase, an amide hydrolase enzyme (E.C.3.5.1.4) with acyl transferase activity, was encapsulated in a reversed micellar system composed of the cationic surfactant tetradecyltrimethyl ammonium bromide (TTAB) in heptane/octanol (80/20%) and phosphate buffer at w₀ 11. The reaction used to study the effect of the reversed micellar system on the enzyme behaviour was a transamidation reaction. The effect of surfactant concentration, buffer molarity and pH on the enzyme kinetics was evaluated. Both initial velocities and product yield were measured. The results indicated that a high initial velocity of hydroxamic acid synthesis and also the highest yield (98%) were obtained using the lowest pH value. The effect of TTAB concentration was dependent on the buffer molarity used. The effect of buffer molarity on reversed micelle dimensions was analysed by light scattering. These results showed that the buffer molarity had a strong influence on the reversed micelle radius that correlated with enzyme activity.     

Protein extration from an aqueous phase into a reversed micellar phase: Effect of water content and reversed micellar composition

In the system composed of the cationic surfactant TOMAC (10 mM), the nonionic (co)surfactant Rewopal HV5 (2 mM), and octanol (0.1% v/v) in isooctane, reversed micelles are formed upon contact with an aqueous phase containing 50 mM ethylene diamine. alpha-Amylase can be transferred from the aqueous phase into reversed micelles in the pH range 9.5 to 10.5 and re-extracted into a second aqueous phase of different composition. The size of the reversed micelles (as reflected in the water content of the organic phase) can be varied by changes in percentage of octanol, type of counterion in the aqueous phase, or in the number of ethoxylate head groups of the nonionic surfactant. An increase in size results in transfer at lower pH values. Experiments in which the charge density in the reversed micellar interface was changed by incorporation of charged derivatives of the nonionic surfactant, without influencing the water content, revealed that an increased charge density facilitated transfer, resulting in a broader transfer profile. Replacement of TOMAC by other quaternary ammonium surfactants differing in number and length of tails revealed that, of the 14 surfactants tested, only 2 gave appreciable amounts of transfer. The amount of transfer is related to the dynamics of phase separation of the surfactants: those giving a poor phase separation inactivate the enzyme. This inactivation is caused by electrostatic interactions between the charged surfactant head groups and charged groups on the enzyme. Electrostatic interactions are the first step of transfer, and can result in either incorporation in a reversed micelle, or, if reversed micelle formation is slow, in enzyme inactivation. (c) 1995 John Wiley & Sons, Inc.     

Affinity-based reversed micellar protein extraction: II. effect of cosurfactant tail length

The selectivity of protein extraction by reversed micellar solutions can be improved by the addition of affinity cosurfactants bearing ligands which bind strongly to the target protein. The interactions between cosurfactant and protein, as well as the interfacial activity of both the free cosurfactant and the protein-cosurfactant complex, were accounted for in a model of the affinity-partitioning process. The aqueous phase dissociation constant was used to describe the protein-ligand interactions. The interfacial partition coefficient for several cosurfactant families varied with tail length according to the well-established hydrophobic effect. Control studies with alkylated chymotrypsin showed that when longer hydrophobic tails are irreversibly attached to the protein, the protein partitions more strongly to the reversed micellar phase. In contrast, for reversible protein-cosurfactant binding, the model predicts a maximum in protein uptake when the cosurfactant tail length is varied; the decrease at longer tail lengths is due to the lowered aqueous phase concentration of affinity cosurfactant, resulting in the formation of fewer protein-cosurfactant complexes. This behavior was confirmed experimentally. (c) 1993 John Wiley & Sons, Inc.     

Selective separation and purification of two lipases from chromobacterium viscosum using AOT reversed micelles

Selective separation and purification of two lipases form Chromobacterium viscosum were carried out by liquid-liquid extraction using a reversed micellar system. Optimum parameters for extraction were determined using a 250 mM AOT micellar solution in isooctane. Complete separation of the two lipases was achieved at pH 6.0 with a 50mM potassium phosphate buffer solution containing 50 mM KCI. By adding 2.5% by volume of ethanol to the lipase-loaded micellar solution, 85% of the extracted lipase could be recovered in a new aqueous phase, 50 mM K(2)HPO(4) with 50 mM KCl, at pH 9.0. Lipase A was purified 2.6-fold with a recovery of 86%, and lipase B by 1.5-fold with a recovery of 76%.     

Activation of lignin peroxidase in organic media by reversed micelles

Activation of lignin peroxidase (LIP) in an organic solvent by reversed micelles was investigated. Bis(2-ethylhexyl)sulfosuccinate sodium salt (AOT) was used as a surfactant to form a reversed micelle. Lyophilized LIP from an optimized aqueous solution exhibited no enzymatic activity in any organic solvents examined in this study; however, LIP was catalytically active by being entrapped in the AOT reversed micellar solution. LIP activity in the reversed micelle was enhanced by optimizing either the preparation or the operation conditions, such as water content and pH in water pools of the reversed micelle and the reaction temperature. Stable activity was obtained in isooctane because of the stability of the reversed micelle. The optimal pH was 5 in the reversed micellar system, which shifted from pH 3 in the aqueous solution. The degradation reaction of several environmental pollutants was attempted using LIP hosted in the AOT reversed micelle. Degradation achieved after a 1-h reaction reached 81%, 50%, and 22% for p-nonylphenol, bisphenol A, and 2,4-dichlorophenol, respectively. This is the first report on the utilization of LIP in organic media.     

A steady-state fluorescence study of cutinase microencapsulated in AOT reversed micelles at optimal stability conditions

A steady-state fluorescence study of cutinase was performed to evaluate the structure of cutinase in reversed micelles of AOT with the optimised conditions assigned by factorial design. The results obtained by two independent methods are compared. At a W₀ (water to surfactant ratio) value of 2.7, and in the presence of 500 mM hexanol, the fluorescence intensity maximum (_max) remained almost constant for a period of time longer than 30.5 h and a slight red-shift from 305 to 310 nm was verified changing the W₀ value to 6. Decreasing the amount of hexanol to 100 mM, the changes in _max were more significant, especially for W₀=6 indicating a noticeable unfolding process. Structural evidence is given reinforcing the role of hexanol as a stabiliser of microencapsulated cutinase and the effect of a drastic reduction in water content.     

Continuous extraction of xylanase from Penicillium janthinellum with reversed micelles using experimental design mathematical model

Xylanase recovery from Penicillium janthinellum with a reversed micellar system consisting of a cationic surfactant using continuous process was evaluated. A statistical approach was applied to the results and showed that the highest xylanase recovery (140%), indicated by the model, was attained at an ionic strength of 7.5 mS cm^–1 and volumetric flow of 0.6 ml min^–1. A new xylanase extraction was performed under these conditions to test the model and showed a close similarity between the experimental result and the value predicted by the model.     

Continuous glycerolysis of olive oil by Chromobacterium viscosum lipase immobilized in liposome in reversed micelles

Chromobacterium viscosum lipase which has adsorbed on liposome and solubilized in microemulsion droplets of glycerol containing a little amount of water could catalyze the glycerolysis of olive oil. Studies on the continuous glycerolysis of olive oil by the immobilized enzyme was done at 37 degrees C in continuous stirred vessel bioreactor with polysulfone membrane. The effect of the flow rate of substrate (olive oil) in isooctane on the conversion and composition of the outlet was investigated using high-performance liquid chromatography (HPLC). The conversion increased with decrease in the flow rate. And we studied the effect of water content in the glycerol-water-lipase solution on the glycerolysis reaction. The conversion to desirable products, mono- and di-olein, was improved without a substantial production of oleic acid at lower water concentrations, i.e., below 8.0% (w/v) which corresponds to a w(o) value of 0.97. At water concentration higher than 8.0% (w/v), the amount of free fatty acid was dramatically increased. Higher operational stability of the enzyme reactor, and the half-line of the enzyme continuous reaction was about 7 weeks.     

Kinetics, mechanism, and time course analysis of lipase-catalyzed hydrolysis of high concentration olive oil in AOT-isooctane reversed micelles

Candida rugosa lipase has been used to investigate the hydrolysis of high concentration olive oil in the AOT-isooctane reversed micellar system at W(o) = 10, pH 7.1, and 37 degrees C. Results from this work show the hydrolytic reaction obeys Michaelis-Menten kinetics up to the initial substrate concentration of 1.37M, with turnover number k(cat) and Michaelis constant K(M) of 67.1 mumol/min mg enzyme and 0.717M, respectively. A competitive inhibition by the main product, oleic acid, has been found with a dissociation constant K(I) for the complex EP* of 0.089M. The rate equation was further analyzed in the time course reaction and was found in agreement with the experimental results for lower substrate concentrations, up to 0.341M. Large deviation occurred at high substrate concentrations, which may be due to the effects of large consumption of water on kinetics, on the formation of glycerol, and on the deactivation of lipase in the hydrolysis reaction as well.     

Liquid-liquid extraction of lectin from Cratylia mollis seeds using reversed micelles

Extraction of lectin from seeds ofCratylia mollis, camaratu bean, with reversed micelles of 100 mM sodium di(2-ethylhexyl) sulfosuccinate/isooctane was performed firstly with affinity-purified lectin. The best conditions were extraction of the seed extract at pH 5 and back-extraction at pH 10, giving yields of 38% and 100%, respectively.     

反胶束萃取酶蛋白的研究进展

反胶束萃取是一项新的分离技术,不仅具有高选择性,而且不易使酶蛋白失活,在提取纯化生物活性物质方面具有巨大的工业应用潜力。本文综述了近年来该方面研究的新进展。     

Enhanced chemiluminescence in the oxidation of luminol and an isoluminol cortisol conjugate by hydrogen peroxide in reversed micelles

The chemiluminescent oxidation of luminol and an isoluminol cortisol conjugate (ABICOR) by hydrogen peroxide has been studied in cetyltrimethylammonium bromide (CTAB) reversed micelles in octane-chloroform (1 : 1). The maximum chemiluminescence intensity of both compounds is dependent on the initial concentrations of the H₂O₂ and substrates, the pH value of the micelle polar phase and the H₂O/CTAB ratio. The optimum pH ranged from 8.5 to 9.5. Under comparable conditions, the chemiluminescence intensity for luminol was 15-fold higher than for the ABI-COR conjugate. A mechanism of oxidation of the substrates in reversed micelles is proposed and the possible mechanisms of inhibition by the substrate and oxidant is discussed.