Purification of lysozyme by affinity-based reversed micellar two-phase extraction

A dye-affinity reversed micellar system was used for lysozyme purification from a crude solution of chicken egg white. The dye-affinity reversed micelles consisted of Cibacron Blue F-3GA (CB; 0.1 mM) modified lecithin (50 g/l) in n-hexane. Starting with a crude egg white solution containing lysozyme of 0.0381 mg/mg protein, lysozyme purity was increased by 16 to 20 times, reached 0.62 to 0.76 mg/mg protein. The affinity micellar system was recycled and used three times. Addition of polyoxyethylene (20) sorbitan trioleate (Tween 85) as a cosurfactant could increase the capacity of the affinity-based reversed micelles. A lysozyme recovery yield of over 70% was obtained at a forward aqueous phase pH of 9.16 using the reversed micelles additionally containing 20 g/l of Tween 85.     

Extraction of monoclonal antibodies (IgG1) using anionic and anionic/nonionic reverse micelles

Purification schemes for antibody production based on affinity chromatography are trying to keep pace with increases in cell culture expression levels and many current research initiatives are focused on finding alternatives to chromatography for the purification of Monoclonal antibodies (MAbs). In this article, we have investigated an alternative separation technique based on liquid–liquid extraction called the reverse micellar extraction. We extracted MAb (IgG1) using reverse micelles of an anionic surfactant, sodium bis 2‐ethyl‐hexyl sulfosuccinate (AOT) and a combination of anionic (AOT) and nonionic surfactants (Brij‐30, Tween‐85, Span‐85) using isooctane as the solvent system. The extraction efficiency of IgG1 was studied by varying parameters, such as pH of the aqueous phase, cation concentration, and type and surfactant concentration. Using the AOT/Isooctane reverse micellar system, we could achieve good overall extraction of IgG1 (between 80 and 90%), but only 30% of the bioactivity of IgG1 could be recovered at the end of the extraction by using its binding to affinity chromatography columns as a surrogate measure of activity. As anionic surfactants were suspected as being one of the reasons for the reduced activity, we decided to combine a nonionic surfactant with an anionic surfactant and then study its effect on the extraction efficiency and bioactivity. The best results were obtained using an AOT/Brij‐30/Isooctane reverse micellar system, which gave an overall extraction above 90 and 59% overall activity recovery. An AOT/Tween‐85/Isooctane reverse micellar system gave an overall extraction of between 75 and 80% and overall activity recovery of around 40–45%. The results showed that the activity recovery of IgG1 can be significantly enhanced using different surfactant combination systems, and if the recovery of IgG1 can be further enhanced, the technique shows considerable promise for the downstream purification of MAbs. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

A metal‐chelate affinity reverse micellar system for protein extraction

A new nonionic reverse micellar system is developed by blending two nonionic surfactants, Triton X‐45 and Span 80. At total surfactant concentrations lower than 60 mmol/L and molar fractions of Triton X‐45 less than 0.6, thermodynamically stable reverse micelles of water content (W₀) up to 30 are formed. Di(2‐ethylhexyl) phosphoric acid (HDEHP; 1–2 mmol/L) is introduced into the system for chelating transition metal ions that have binding affinity for histidine‐rich proteins. HDEHP exists in a dimeric form in organic solvents and a dimer associated with one transition metal ion, including copper, zinc, and nickel. The copper‐chelate reverse micelles (Cu‐RM) are characterized for their W₀, hydrodynamic radius (R_h), and aggregation number (N_ag). Similar with reverse micelles of bis‐2‐ethylhexyl sodium sulfosuccinate (AOT), R_h of the Cu‐RM is also linearly related to W₀. However, N_ag is determined to be 30–90 at W₀ of 5–30, only quarter to half of the AOT reverse micelles. Then, selective metal‐chelate extraction of histidine‐rich protein (myoglobin) by the Cu‐RM is successfully performed with pure and mixed protein systems (myoglobin and lysozyme). The solubilized protein can be recovered by stripping with imidazole or ethylinediaminetetraacetic acid (EDTA) solution. Because various transition metal ions can be chelated to the reverse micelles, it is convinced that the system would be useful for application in protein purification as well as simultaneous isolation and refolding of recombinant histidine‐tagged proteins expressed as inclusion bodies. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

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.     

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.     

Equilibria and kinetics of protein transfer to and from affinity-based reverse micelles of Span 85 modified with Cibacron Blue F-3GA

Sorbitan trioleate was modified with Cibacron Blue F-3GA (CB) to create an affinity surfactant and to form affinity-based reverse micelles in n-hexane. The partitioning equilibria and the extraction kinetics of lysozyme and bovine serum albumin (BSA) were then examined. The solubilization capacity of the reverse micellar system for lysozyme increased linearly with increasing the CB concentration from 0.1 to 0.5 mmol L⁻¹. In contrast, the capacity for BSA at 0.5 mmol L⁻¹ of coupled CB was only about one-fifth that for lysozyme. It indicates a strong steric hindrance effect of the micelles for the high molecular mass protein. The overall volumetric mass transfer coefficient of lysozyme in the forward extraction increased from 0.43 × 10⁻³ to 1.25 × 10⁻³ s⁻¹ with increasing CB concentration from 0.1 to 0.5 mmol L⁻¹. Due to the high molecular mass of BSA, its volumetric mass transfer coefficient in the forward extraction was only one-sixth that of lysozyme. The ratio of the coefficient in the back extraction to that in the forward extraction was less than 0.03, much lower than those in other micellar systems. It indicates that the interfacial resistance in this system was severer than in others.     

Effect of hexanol as a cosolvent on partitioning and mass transfer rate of protein extraction using reversed micelles of CB-modified lecithin

Using the affinity-based reversed micelles composed of Cibacron Blue F3G-A (CB) modified soybean lecithin, the effect of hexanol as a cosolvent on the extraction of lysozyme and bovine serum albumin (BSA) was investigated. The water concentration in the reversed micelles increased significantly with increasing hexanol concentration. The partition coefficient of lysozyme could be increased by over 12-fold by introducing hexanol of higher than 0.5 vol%. However, the transfer of BSA was hardly affected because its high molecular weight resulted in a strong steric hindrance effect. The enzymatic activity of lysozyme was nearly 100% retained after undergoing the extraction process with the CB–lecithin micelles containing 3 vol% hexanol. The partitioning isotherms of lysozyme in the CB–lecithin micelles with and without hexanol addition were expressed by the Langmuir equation. The partitioning capacity of lysozyme was nearly increased twofold by introducing 3 vol% hexanol to the CB–lecithin micelles and reached 2.12 g/l. The cosolvent hexanol revealed insignificant effect on the mass transfer rate, and in both the systems with and without hexanol, the mass transfer rate in back extraction was 5–10 times slower than that in the forward extraction. This phenomenon was similar to that in conventionally employed ionic surfactant systems. The result suggests that in the present affinity-based reversed micelles, the interfacial resistance also played a more important role in back extraction than in forward extraction.     

His‐tagged protein purification by metal‐chelate affinity extraction with nickel‐chelate reverse micelles

Di(2‐ethylhexyl) phosphoric acid (HDEHP) was used as a transition metal ion chelator and introduced to the nonionic reverse micellar system composed of equimolar Triton X‐45 and Span 80 at a total concentration of 30 mmol/L. Ni(II) ions were chelated to the HDEHP dimers in the reverse micelles, forming a complex denoted as Ni(II)R₂. The Ni(II)‐chelate reverse micelles were characterized for the purification of recombinant hexahistidine‐tagged enhanced green fluorescent protein (EGFP) expressed in Escherichia coli. The affinity binding of EGFP to Ni(II)R₂ was proved by investigation of the forward and back extraction behaviors of purified EGFP. Then, EGFP was purified with the affinity reverse micelles. It was found that the impurities in the feedstock impeded EGFP transfer to the reverse micelles, though they were little solubilized in the organic phase. The high specificity of the chelated Ni²⁺ ions toward the histidine tag led to the production of electrophoretically pure EGFP, which was similar to that purified by immobilized metal affinity chromatography. A two‐stage purification by the metal‐chelate affinity extraction gave rise to 87% recovery of EGFP. Fluorescence spectrum analysis suggests the preservation of native protein structure after the separation process, indicating the system was promising for protein purification. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Enzymatic hydrolysis of microcrystalline cellulose in reverse micelles

The activities of cellulases from Trichoderma reesei entrapped in three types of reverse micelles have been investigated using microcrystalline cellulose as the substrate. The reverse micellar systems are formed by nonionic surfactant Triton X-100, anionic surfactant Aerosol OT (AOT), and cationic surfactant cetyltrimethyl ammonium bromide (CTAB) in organic solvent media, respectively. The influences of the molar ratio of water to surfactant omega0, one of characteristic parameters of reverse micelles, and other environmental conditions including pH and temperature, on the enzymatic activity have been studied in these reverse micellar systems. The results obtained indicate that these three reverse micelles are more effective than aqueous systems for microcrystalline cellulose hydrolysis, and cellulases show "superactivity" in these reverse micelles compared with that in aqueous systems under the same pH and temperature conditions. The enzymatic activity decreases with the increase of omega0 in both AOT and Triton X-100 reverse micellar systems, but reaches a maximum at omega0 of 16.7 for CTAB reverse micelles. Temperature and pH also influence the cellulose hydrolysis process. The structural changes of cellulases in AOT reverse micelles have been measured by intrinsic fluorescence method and a possible explanation for the activity changes of cellulases has been proposed.     

Bioaffinity separation of chymotrypsinogen using antigen-antibody reaction in reverse micellar system composed of a nonionic surfactant

Selective separation of chymotrypsinogen using anti-chymotrypsinogen-antibodies as affinity ligands was realized in reverse micellar system composed of a nonionic surfactant tetra-oxyethylenemonodecylether. Antibodies as affinity ligands were immobilized in reverse micelles by combining cholesteryl groups covalently. Selective separation of proteins using bioaffinity ligands was extended to antigen-antibody reaction system, which enables us to choose any kind of target proteins.     

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.     

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.     

人源溶菌酶在大肠杆菌中的表达与复性研究

人源溶菌酶(Human lysozyme,HLZ)是一种糖苷水解酶,具有抗菌消炎的作用,其作为抗生素的替代品,已经被广泛应用于食品业、畜牧业和医疗等领域。如何获得高产量、高活性、高纯度的人源溶菌酶一直是亟待解决的技术问题。优化人源溶菌酶编码基因密码子,提高其在大肠杆菌中的适应度和表达量;将优化的基因克隆至大肠杆菌表达质粒pET21a,并将其在大肠杆菌表达菌株BL21(DE3)中诱导表达;利用8 mol/L尿素溶液对包涵体进行溶解变性后,探究一步透析、梯度透析和梯度稀释3种复性方式以及复性液中谷胱甘肽氧化还原对(GSSG/GSH)、精氨酸、甘油等复性物的浓度对重组人源溶菌酶复性的效果,获得最佳的复性方案。研究结果表明:37℃诱导温度下,利用0.5 mmol/L IPTG成功诱导了分子量约为14.7 kD的重组人源溶菌酶的表达,包涵体表达量约为380 mg/L(湿重)。包涵体经一步透析、梯度透析和梯度稀释3种复性方式复性后,测得比活力值分别为147 U/mg、335 U/mg、176 U/mg,表明最佳复性方法为梯度透析复性法。进一步探索了复性液中GSSG/GSH比值、精氨酸浓度、甘油浓度对人源溶菌酶复性效果的影响,表明当复性液中同时添加浓度比为1∶2的GSSG/GSH、4 mmol/L精氨酸和6%甘油时,复性后人源溶菌酶的最佳比活力值为1170 U/mg,显著高于3种复性物均不加时溶菌酶335 U/mg的比活力值,但低于溶菌酶标准品1732 U/mg的比活力值。成功地将人源溶菌酶基因在大肠杆菌中表达,并通过包涵体复性体系成功获得高活性重组人源溶菌酶。     

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.     

Statistical optimization and multiple objective programming of lysozyme refolding catalyzed by recombinant DsbA in vitro

DsbA (disulfide bond formation protein A) is essential for disulfide bond formation directly affecting the nascent peptides folding to the correct conformation in vivo. In this paper, recombinant DsbA protein was employed to catalyze denatured lysozyme refolding and inhibit the aggregation of folding intermediates in vitro. Statistical methods, i.e., Plackett–Burman design and small central composite design, were adopted to screen out important factors affecting the refolding process and correlating these parameters with the refolding efficiency including both protein recovery and specific activity of refolded lysozyme. Four important parameters: initial lysozyme concentration, urea concentration, KCl concentration and GSSG (glutathione disulfide) concentration were picked out and operating conditions were optimized by introducing the effectiveness coefficient method and transforming the multiple objective programming into an ordinary constrained optimization issue. Finally, 99.7% protein recovery and 25,600 U/mg specific activity of lysozyme were achieved when 281.35 μg/mL denatured lysozyme refolding was catalyzed by an equivalent molar of DsbA at the optimal settings. The results indicated that recombinant DsbA protein could effectively catalyze the oxidized formation and reduced isomerization of intramolecular disulfide bonds in the refolding of lysozyme in vitro.     

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.     

Reverse micellar extraction and precipitation of lysozyme using sodium di(2-ethylhexyl) sulfosuccinate

Sodium di(2-ethylhexyl) sulfosuccinate, referred to as Aerosol-OT or AOT, was used to remove lysozyme from an aqueous phase via reverse micellar extraction and precipitation method. For both methods, when the surfactant was in excess, a complete removal of lysozyme from the aqueous phase was obtained at the values of pH below the pI of lysozyme. However, for the reverse micellar method, a solubilization limit of lysozyme in the organic phase was observed, and a white precipitate was formed at the aqueous-organic interface. This observation suggested using AOT directly as a precipitating ligand. The lysozyme precipitated with AOT was fully recovered, with its original enzymatic activity, using acetone as a recovery solvent. A mechanism is suggested to explain the solubilization of lysozyme in an AOT reverse micellar system. It is shown that a direct precipitation method can be used with advantage instead of using the reverse micellar extraction method to recover lysozyme from an aqueous phase.     

Affinity extraction of BSA with reversed micellar system composed of unbound Cibacron Blue

Affinity Cibacron Blue 3GA (CB) dye in aqueous phase was directly transferred to the reversed micelles due to electrostatic interaction between anionic CB and cationic cetyltrimethylammonium bromide (CTAB). The bovine serum albumin (BSA) transfer to the reverse micelles increases significantly in a wide range of pH by the addition of a small amount of CB ( approximately 1.0-7.0% of the total surfactant concentration) to the aqueous phase. For pH < pI, the selectivity can be significantly improved with the presence of affinity CB because no BSA was extracted in the absence of CB. For backward extraction of BSA from the micellar phase with stripping aqueous solution, the addition of 2-propanol to the aqueous phase can recover almost all BSA (98.5%) extracted into the reverse micelles.     

Investigation on the mechanism of crystallization of soluble protein in the presence of nonionic surfactant

The mechanism of crystallization of soluble, globular protein (lysozyme) in the presence of nonionic surfactant C8E4 (tetraoxyethylene glycol monooctyl ether) was examined using both static and dynamic light scattering. The interprotein interaction was found to be attractive in solution conditions that yielded crystals and repulsive in the noncrystallizing solution conditions. The validity of the second virial coefficient as a criterion for predicting protein crystallization could be established even in the presence of nonionic surfactants. Our experiments indicate that the origin of the change in interactions can be attributed to the adsorption of nonionic surfactant monomers on soluble proteins, which is generally assumed to be the case with only membrane proteins. This adsorption screens the hydrophobic attractive force and enhances the hydration and electrostatic repulsive forces between protein molecules. Thus at low surfactant concentration, the effective protein-protein interaction remains repulsive. Large surfactant concentrations promote protein crystallization, possibly due to the attractive depletion force caused by the intervening free surfactant micelles.