Protein refolding by reversed micelles utilizing solid-liquid extraction technique

This article reports that a reversed micellar solution is useful for refolding proteins directly from a solid source. The solubilization of denatured RNase A, which had been prepared by reprecipitation from the denaturant protein solution, into reversed micelles formulated with sodium di-2-ethylhexyl sulfosuccinate (AOT) has been investigated by a solid-liquid extraction system. This method is an alternative to the ordinary protein extraction in reversed micelles based on the liquid-liquid extraction. The solid-liquid extraction method was found to facilitate the solubilization of denatured proteins more efficiently in the reversed micellar media than the ordinary phase transfer method of liquid extraction. The refolding of denatured RNase A entrapped in reversed micelles was attained by adding a redox reagent (reduced and oxidized glutathion). Enzymatic activity of RNase A was gradually recovered with time in the reversed micelles. The denatured RNase A was completely refolded within 30 h. In addition, the efficiency of protein refolding was enhanced when reversed micelles were applied to denatured RNase A containing a higher protein concentration that, in the case of aqueous media, would lead to protein aggregation. The solid-liquid extraction technique using reversed micelles affords better scale-up advantages in the direct refolding process of insoluble protein aggregates.     

Protein refolding in reversed micelles: Interactions of the protein with micelle components

A novel process has been developed to improve the refolding yield of denatured proteins. It uses reversed micelles to isolate denatured protein molecules from each other and thus, upon refolding, reduces the intermolecular interactions which lead to aggregation. The feasibility of this process was first demonstrated with Ribonuclease A as a model protein. In the present work, we expanded the scope of this study to better understand both the general mechanisms of protein refolding in reversed micelles and the biotechnological applicability of the process. First, we investigated the interactions between the individual components of the reversed micellar system (the protein molecule, the denaturant guanidine hydrochloride (GuHCl), and the surfactant (AOT)) during the refolding process. We then extended our studies to a more hydrophobic protein, gamma-interferon, which aggregates upon refolding in aqueous solution. However, it was also found to aggregate in our reversed micelle process during the extraction step. Since gamma-interferon is a much more hydrophobic protein than RNase, we hypothesize that interactions between hydrophobic amino acids and the surfactant layer may interfere with refolding. This hypothesis was tested by studying the refolding of chemically modified RNase. The substitution of 55% of the surface lysine residues with hydrophobic caproyl groups caused a significant decrease in the refolding yield of RNase in the reversed micellar system without affecting aqueous solution renaturation. In addition, the extraction efficiency of the enzyme from reversed micelles back into aqueous solution was severely reduced and resulted in aggregation. These experiments indicate that unfolded hydrophobic Proteinsinteract with the Surfactant molecules, which limits their ability to refold in reversed micelles.     

Direct refolding of inclusion bodies using reversed micelles

The protein refolding of inclusion bodies was investigated using reversed micelles formed by aerosol OT (AOT). Ribonuclease A (RNase A) was overexpressed in Escherichia coli and used as native inclusion bodies. The enzymatic activity of RNase A was completely regained from the inclusion bodies within 14 h by solubilization in reversed micelles. To further enhance the refolding rate, a molecular chaperone, GroEL, was incorporated into the refolding system. The resultant refolding system including GroEL showed better performance under optimized conditions for the refolding of RNase A inclusion bodies. The refolding rate was considerably improved by the addition of the molecular chaperone, and the refolding step was completed in 1 h. The protein refolding in the GroEL-containing refolding system was strongly dependent on the coexistence of ATP and Mg2+, suggesting that the GroEL hosted in the reversed micelles was biologically active and assisted in the renaturation of the inclusion bodies. The addition of cold acetone to the reversed micellar solution allowed over 90% recovery of the renatured RNase A.     

Mechanism of extraction of chymotrypsin into isooctane at very low concentrations of aerosol OT in the absence of reversed micelles

Chymotrypsin is easily extracted from an aqueous solution into isooctane containing the anionic surfactant aerosol OT (AOT). The concentration of AOT needed to efficiently extract 0.5 mg/mL CMT is as low as 1 mM and as low as 0.2 mM AOT was sufficient to extract the protein into isooctane. The extraction process was unaffected by 10% (v/v) ethyl acetate in the isooctane phase. Moreover, spectroscopic analysis by electron paramagnetic resonance indicated that CMT did not exist inside a discreet water pool of a reversed micelle. Calculations of the number of AOT molecules associated per extracted CMT molecule indicate that only ca. 30 surfactant molecules interact with the protein, a value too low for reversed micellar incorporation of the protein in isooctane. These studies suggested that reversed micelles do not need to be involved in the actual transfer of the protein from the aqueous to the organic phase and protein solubilization in the organic phase is possible in the absence of reversed micelles. Based on these findings, a new mechanism has been proposed herein for protein extraction via the phase transfer method involving ionic surfactants. The central theme of this mechanism is the formation of an electrostatic complex between CMT and AOT at the aqueous/organic interface between AOT and CMT, thereby leading to the formation of a hydrophobic species that partitions into the organic phase. Consistent with this mechanism, the efficiency of extraction is dependent on the interfacial mass transfer, the concentrations of CMT and AOT in the aqueous and organic phases, respectively; the ionic strength of the aqueous phase; and the presence of various cosolvents. (c) 1994 John Wiley & Sons, Inc.     

Protein refolding in reversed micelles

A novel process has been developed which uses reversed micelles to isolate denatured protein molecules from each other and allows them to refold individually. These reversed micelles are aqueous phase droplets stabilized by the surfactant AOT and suspended in isooctane. By adjusting conditions such that only one protein molecule is present per reversed micelle, it was possible to achieve independent folding without encountering the problem of aggregation due to interactions with neighboring molecules. The feasibility of this process was demonstrated using bovine pancreatic ribonuclease A as a model system. It was shown that denatured and reduced ribonuclease can be transferred from a buffered solution containing guanidine hydrochloride into reversed micelles to a greater extent than native enzyme under the same conditions. The denaturant concentration can then be significantly reduced in the reversed micellar phase, while retaining most of the protein, by means of extractive contacting stages with a denaturant-free aqueous solution. Denatured and reduced ribonuclease will subsequently recover full activity inside reversed micelles within 24 h upon addition of a mixture of reduced and oxidized glutathione to reoxidize disulfide bonds. Extraction of this refolded enzyme from reversed micelles back into aqueous solution can be accomplished by contacting the reversed micelle phase with a high ionic strength (1.0M KCl) aqueous solution containing ethyl acetate.     

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.     

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.     

Studies on the extraction and back-extraction of a recombinant cutinase in a reversed micellar extraction process

This work deals with the extraction and back-extraction of a recombinant cutinase using AOT reversed micelles in isooctane. The effect of pH, ionic strength, AOT concentration and temperature on the extraction and back-extraction of the cutinase was investigated. High extraction (97%) of the cutinase was achieved at pH 7.0 with a 50 mM Tris-HCl buffer solution containing 100 mM KCl, but a low activity was detected in the reversed micellar phase. At pH 9.0, cutinase was extracted (75%) to the reversed micelles with higher activity. Cutinase was recovered (50%) from a reversed micellar phase (100 mM AOT/isooctane) into a 50 mM Tris-HCl buffered solution at pH 9.0 with 100 mM KCl, and 20°C. Protein and cutinase activity global yields of 38 and 45%, respectively, were obtained for the global process, extraction and back-extraction steps, using low ionic strength, pH 9.0, 100 mM AOT and 20°C.Maria das Graças Carneiro da Cunha acknowledges a Ph.D. fellowship from Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq) and Centro de Pesquisas Aggeu Magalhães, Brasil. This work was partly financed by the BRIDGE Programme (Contract BIOT-CT91-0274(DTEE)).     

Efficacy of guanidium salts in protein recovery from reverse micellar organic media

The efficacy of guanidium salts in the recovery of extracted lysozyme from aerosol-OT (AOT) reverse micellar organic phase was investigated. Adding guanidium salt at a low concentration as pretreatment reagent in the feed solution led to successful protein recovery, and the enzymatic activity of the recovered lysozyme was well maintained. Among the electrolytes tested, caotropic guanidine thiocyanate (GuHSCN) was the most effective in recovering lysozyme as well as in preserving its activity. The presence of guanidium salt in the micellar organic phase markedly lowered the water content, apparently by reducing or eliminating accompanying water arising from lysozyme solubilization. CD data showed that the α-helix content of the lysozyme in the micellar phase in the presence of dilute guanidium salt was smaller than that in a guanidium-free micellar phase. These results indicated that the guanidium salt expelled lysozyme molecules from the micro-interface of the reverse micelles into the hydrophilic micro-water pool.     

Study of the factors affecting the extraction of soybean protein by reverse micelles

In this work, the forward and back extraction of soybean protein by reverse micelles was studied. The reverse micellar systems were formed by anionic surfactant sodium bis(2-ethyl hexyl) sulfosuccinate (AOT), isooctane and KCl solution. The effects of AOT concentration, aqueous pH, KCl concentration and phase volume ratio on the extraction efficiency of soybean protein were tested. Suitability of reverse micelles of AOT and Triton-X-100/AOT mixture in organic solvent toluene for soybean protein extraction was also investigated. The experimental results lead to complete forward extraction at the AOT concentration 120 mmol l⁻¹, aqueous pH 5.5 and KCl concentration 0.8 mol l⁻¹. The backward extraction with aqueous phase (pH 5.5) resulted in 100% extraction of soybean protein from the organic phase.     

Renaturation and interaction of ribonuclease A with AOT surfactant in reverse micelles

This study extended works on effects of solute on the percolation of reverse micelles to the effects of interactions between protein and surfactants on protein refolding by reverse micelles. The changes in percolation behavior were identified and attributed to the position of solutes in the core aqueous phase and the interaction between the solute and the surfactants. The percolation behavior of reverse micelles with solutes was related to protein renaturation and the reverse micelle. This study aims to highlight the involvement of the interface and the interaction of the protein with the surfactant during protein refolding. Ribonuclease A and AOT reverse micelles together constitute a model system considered here. The systemic parameters of the reverse micelle, water content (W(o)) and pH value, were applied to modify the interaction between the denatured protein molecules and the surfactant interface. The interactions and the locations of the protein molecules were determined from changes in percolation temperature measured by conductivity. The percolation and protein activity show that a stronger interaction of the protein molecules with surfactant corresponds to superior recovery of protein activity. The investigation concludes that the refolding of protein by reverse micelles is not only facilitated by the isolation of reverse micelles but also by the interaction due to the interface of the reverse micelle.     

Nonaggregating refolding of ribonuclease A using reverse micellar dialysis

A hydrophilic ultrafiltration membrane, regenerated cellulose, facilitates the size-selectable permeability of hydrophilic solutes in reverse micellar solution. By using an ultrafiltration membrane with a molecular weight cutoff of 3,500, we demonstrate a nonaggregating protein refolding technique based on the dialysis of reverse micellar solution. This realizes concurrent removal of denaturants, urea and 2-mercaptoethanol, and the supply of redox reagents, reduced and oxidized glutathione (GSH, GSSG), to promote renaturation of proteins. Two mg/ml ribonuclease A (RNase A) was refolded completely without any dilution and aggregation for 60 h. The refolding behavior of RNase A is strongly influenced by the ratio of GSH and GSSG. Moreover, we recovered 90% of the refolded RNase A from AOT reverse micellar solution with acetone precipitation and beta-cyclodextrin washing. These findings should facilitate the production of a continuous protein refolding membrane reactor.     

Development of a new reversed micelle liquid emulsion membrane for protein extraction

A new type of liquid emulsion membrane containing reversed micelles for protein extraction is introduced. A three-step extraction mechanism is proposed including solubilization, transportation, and release of the protein. The surfactants Span80 and sodium di(2-ethylhexyl)sulfosuccinate (AOT) are used to stabilize the membrane phase and to build up the reversed micelles, respectively. alpha-Chymotrypsin was used as the model protein. The condition in the internal phase inhibits the solubilization process of the already extracted protein back into reversed micelles. Concerning the solubilization, we studied the influence of the AOT concentration in the membrane phase and the ionic strength in the external phase. The extraction rate increases with higher AOT concentration and decreases with higher ionic strength. Using NaCl in the external phase led to better extraction results than using KCl. Maximum extraction results of 98% into the membrane phase and 65% into the internal phase were obtained. This condition retained 60% of the enzyme's activity. The concentration of KCl in the internal phase does not affect the solubilization rate but the release into the internal phase. By this way the ionic strength in the internal phase is used as the driving force for the protein release. The solubilization process is much faster than the diffusion and the releasing process, as found by variation of the extraction time. The influence of the operating conditions on the membrane swelling is also discussed. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 267-273, 1997.     

Characterization of lipase in reversed micelles formulated with cibacron blue F-3GA modified span 85

Sorbitan trioleate (Span 85) modified by Cibacron Blue F-3GA (CB) was prepared and used as an affinity surfactant to formulate a reversed micellar system for Candida rugosa lipase (CRL) solubilization. The system was characterized and evaluated by employing CRL-catalyzed hydrolysis of olive oil as a model reaction. The micellar hydrodynamic radius results reflected, to some extent, the redistribution of surfactant and water after enzyme addition, and the correlation between surfactant formulation, water content (W0), micellar size, and enzyme activity. An adequate modification density of CB was found to be important for the reversed micelles to retain enough hydration capacity and achieve high enzyme activity. Compared with the results in AOT-based reversed micelles, CRL in this micellar system exhibited a different activity behavior versus W0. The optimal pH and temperature of the encapsulated lipase remained unchanged, but the apparent activity was significantly higher than that of the native enzyme in bulk solution. Kinetic studies indicated that the encapsulated lipase in the reversed micelles of CB-formulated Span 85 followed the Michaelis-Menten equation. The Michaelis constant was found to decrease with increasing surfactant concentration, suggesting an increase of the enzyme affinity for the substrate. Stability of the lipase in the reversed micelles was negatively correlated to W0.     

Forward and backward extraction rates of amino acid in reversed micellar extraction

The mass transfer characterization in reversed micellar extraction of amino acid phenylalanine (Phe) is presented. The mass transfer rates in forward extraction of Phe from aqueous KCl solutions (pH 1.4 – 2.3) to AOT/isooctane reversed micellar solutions and in backward extraction from the reversed micellar organic phase to KHCO₃/KOH buffer solutions (pH 9.0 – 11.0) were investigated using a stirred cell with a flat liquid–liquid interface. Both the forward and the backward extraction rates are controlled by the interfacial rate processes, i.e., the solubilization and the release processes. The solubilizing rate constants for the forward extraction of Phe increase with decreasing pH and initial Phe concentration and with increasing initial AOT concentration. On the other hand, the releasing rate constants for the backward extraction decrease with increasing initial AOT concentration and with decreasing ionic strength, but are little influenced by pH. The backward extraction rates are fairly slow compared to the forward extraction rates, and are accelerated by the addition of 2-methyl-2-propanol, similar to the extraction of protein lysozyme.     

Spectroscopic properties of horse liver alcohol dehydrogenase in reversed micellar solutions

Catalytic and spectroscopic properties of alcohol dehydrogenase from horse liver, incorporated in reversed micellar media, have been studied. Two different reversed micellar systems have been used, one containing an anionic [sodium bis(2-ethylhexyl)sulfosuccinate, AOT], the other containing a cationic (cetyltrimethylammonium bromide, CTAB) surfactant. With 1-hexanol as substrate the turnover number of the enzyme in AOT-reversed micelles is strongly dependent on the water content of the system. At low wo ([H2O]/[surfactant]) (wo less than 20) no enzymatic activity can be detected whereas at high wo (wo = 40) the turnover is only slightly lower than in aqueous solution. In CTAB-reversed micelles the dependence of the turnover number on wo is much less. The enzymatic activity is in this case significantly lower than in aqueous solution and increases only slightly with an increasing water content of the reversed micelles. Possible interactions of the protein with the surfactant interfaces in the reversed micellar media were studied via circular dichroism and fluorescence measurements. From the circular dichroism of the protein backbone it is observed that the protein secondary structure is not significantly affected upon incorporation in the reversed micelles since the far-ultraviolet spectrum is not altered. Results from time-resolved fluorescence anisotropy experiments indicate that, especially in AOT-reversed micelles, interactions between the protein and the surfactant interface are largely electrostatic in nature, as evident from the dependence on the pH of the buffer used. In CTAB-reversed micellar solutions such interactions appear to be much less pronounced than in AOT.     

Affinity extraction of proteins with a reversed micellar system composed of Cibacron Blue-modified lecithin

Crude soybean lecithin was used as a novel surfactant to form reversed micelles in n-hexane. Cibacron Blue F-3GA (CB) was directly immobilized to the reversed micelles by a two-phase reaction. The reversed micellar system without CB showed low solubilizing capacity for low molecular weight proteins, lysozyme, and cytochrome c due to the weak electrostatic interactions. The introduction of CB significantly increased the solubilization of lysozyme because of its affinity binding to CB but showed no effect on the solubilization of cytochrome c since it did not bind to CB. Although bovine serum albumin had an affinity for CB, it was not extracted to the reversed micelles containing CB because its high molecular weight resulted in a significant steric hindrance effect. Thus the reversed micellar system had a high selectivity resulting from both biospecific and steric hindrance effects. The extraction yield of lysozyme decreased significantly with increasing ionic strength. Therefore, the back extraction of lysozyme was carried out using a stripping solution with an ionic strength of 0.865 mol/L. The overall recovery yield of lysozyme after back extraction could be increased to 87% by stripping for 2 h. The recovered lysozyme exhibited an activity equivalent to native lysozyme, and its secondary structure was also unchanged.     

Characteristics of antigen-antibody interaction in the reversed micelles of surface-active agents in heptane

The alterations in the catalytic activity of the horseradish peroxidase after its interaction with antibodies against this enzyme have been studied in buffered solution and in reversed Aerosol OT (AOT) micelles in heptane. The antibodies were obtained by immunizing the rabbits with electrophoretically homogeneous enzyme and were purified by affinity chromatography. In the AOT micelles and mixed micelles containing AOT and Triton X-45, the enzyme interacted with antibodies very rapidly (in less than 5 min), i.e. the micelles did not hinder effective interaction between the enzyme and antibodies. The decrease in the peroxidase catalytic activity upon its interaction with antibodies in a micellar medium was determined by [H2O]/[AOT] ratio, pH and molarity of polar nucleus, as well as by the initial concentration of antibody. In buffered solutions, the decrease n the peroxidase activity of the enzyme--antibody complex was only weakly dependent on pH and molarity of a buffer solution.     

Partitioning behavior and enrichment of proteins with reversed micellar extraction: I. forward extraction of proteins from aqueous to reversed micellar phase

Protein extractions using aerosol OT (AOT)-isooctane reverse micelle solutions have been studied to explore the potential for separating and enriching proteins with the reversed micellar extraction. The effects of pH, ionic strength, and different cations of chlorides in a bulk aqueous phase and of AOT concentration in an organic phase on the partitioning of lysozyme and myoglobin and the solubilization of water are presented in detail. The extraction of lysozyme was affected by the concentration of potassium or barium but was almost independent of that of sodium or calcium, whose ionic diameter is smaller than that of potassium and barium. For the extraction of myoglobin, however, the effect of barium concentration was not appreciable. Lysozyme could be enriched into the reversed micellar phase up to 30 times the aqueous feed concentration. (c) 1993 John Wiley & Sons, Inc.