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.     

Modeling of protein refolding from inclusion bodies

Overexpression of foreign proteins in Escherichia coli often leads to the formation of inclusion bodies （IBs）, which becomes the major bottleneck in the preparation of recombinant proteins and their applications. In the present study, 36 proteins from IBs were refolded using a simple refolding method. Refolding yields of these proteins were defined as the percentage of soluble pro- teins following dilution refoiding in the amount of denatured proteins in the samples before diluting into refolding buffer. Furthermore, a mathematical model was deduced to evaluate the role of biochemical proper- ties in the protein refolding. Our results indicated that under the experimental conditions, isoelectric point of proteins might be mostly contributing to the high effi- cacy of protein refolding since the increment of one unit resulted in a decrease of 14.83% in the refolding yield. Other important mediators were components of protein secondary structure and the molecular weight （R2= 0.98, P = 0.000, F-test）. Six proteins with low efficiency in the protein refolding possessed relatively low isoelectric points. Furthermore, refolding yields of six additional proteins from IBs were predicted and further validated by refolding the proteins under the same conditions. Therefore, the model of protein refold- ing developed here could be used to predict the refold- ing yields of proteins from IBs through a simple method. Our study will be suggestive to optimize the methods for protein refoiding from IBs according to their intrinsic properties.     

High-throughput automated refolding screening of inclusion bodies

One of the main stumbling blocks encountered when attempting to express foreign proteins in Escherichia coli is the occurrence of amorphous aggregates of misfolded proteins, called inclusion bodies (IB). Developing efficient protein native structure recovery procedures based on IB refolding is therefore an important challenge. Unfortunately, there is no "universal" refolding buffer: Experience shows that refolding buffer composition varies from one protein to another. In addition, the methods developed so far for finding a suitable refolding buffer suffer from a number of weaknesses. These include the small number of refolding formulations, which often leads to negative results, solubility assays incompatible with high-throughput, and experiment formatting not suitable for automation. To overcome these problems, it was proposed in the present study to address some of these limitations. This resulted in the first completely automated IB refolding screening procedure to be developed using a 96-well format. The 96 refolding buffers were obtained using a fractional factorial approach. The screening procedure is potentially applicable to any nonmembrane protein, and was validated with 24 proteins in the framework of two Structural Genomics projects. The tests used for this purpose included the use of quality control methods such as circular dichroism, dynamic light scattering, and crystallogenesis. Out of the 24 proteins, 17 remained soluble in at least one of the 96 refolding buffers, 15 passed large-scale purification tests, and five gave crystals.     

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.     

Important parameters affecting efficiency of protein refolding by reversed micelles

Refolding of denatured RNase A as a model of inclusion bodies was performed by reversed micelles formulated with sodium di-2-ethylhexyl sulfosuccinate (AOT) in isooctane. In the novel refolding process, a solid-liquid extraction was utilized as an alternative to the ordinary protein extraction by reversed micelles based on a liquid-liquid extraction. First, the effects of operational parameters such as concentration of AOT, W(o) (= [H(2)O]/[AOT]), and pH were examined on the solubilization of solid denatured proteins into a reversed micellar solution. The solubilization was facilitated by a high AOT concentration, a high W(o) value, and a high pH in water pools. These conditions are favorable for the dispersion of the solid protein aggregates in an organic solvent. Second, the renaturation of the denatured RNase A solubilized into the reversed micellar solution was conducted by addition of glutathione as a redox reagent. A complete renaturation of RNase A was accomplished by adjusting the composition of the redox reagent even at a high protein concentration in which protein aggregation would usually occur in aqueous media. In addition, the renaturation rates were improved by optimizing water content (W(o)) and the pH of water pools in reversed micelles. Finally, the recovery of renatured RNase A from the reversed micellar solution was performed by adding a polar organic solvent such as acetone into the reversed micellar solution. This precipitation method was effective for recovering proteins from reversed micellar media without any significant reduction in enzymatic activity.     

Practical considerations in refolding proteins from inclusion bodies

Refolding of proteins from inclusion bodies is affected by several factors, including solubilization of inclusion bodies by denaturants, removal of the denaturant, and assistance of refolding by small molecule additives. We will review key parameters associated with (1) conformation of the protein solubilized from inclusion bodies, (2) change in conformation and flexibility or solubility of proteins during refolding upon reduction of denaturant concentration, and (3) the effect of small molecule additives on refolding and aggregation of the proteins.     

On-column refolding of recombinant human interleukin-4 from inclusion bodies

Interleukin-4 (IL4) is a multifunctional cytokine which plays a key role in the immune system. Several antagonists/agonists of IL4 are reported through mutagenesis studies, but their solution structural studies using nuclear magnetic resonance (NMR) spectroscopy are hindered as milligram quantities of isotopically labeled protein are required for structural refinements. In this work, a His-tagged recombinant form of human IL4 was overexpressed in Escherichia coli under the control of a T7 promoter. The resulting inclusion bodies were separated from cellular debris by centrifugation and solubilized by 6M guanidine-HCl in the presence of reducing agents. The denatured IL4 was immobilized on Ni2+-fractogel beads and refolded in a single chromatographic step by gradual removal of denaturant. This protocol yielded 15-20 mg of isotope-enriched protein from 1L of culture grown in minimal medium. The refolded protein was highly pure and was correctly folded as judged by its two-dimensional NMR spectrum. To show the successful application of this refolding protocol to IL4 variants, 15N-labeled Y124D-IL4 was also prepared and its first two-dimensional NMR spectrum was presented.     

TRAIL包涵体在细胞内重折叠现象的初步研究

肿瘤坏死因子相关凋亡诱导配体（Ap02L／TRAIL）是一种新型的抗肿瘤蛋白。但在大肠杆菌表达系统中,表达的TRAIL蛋白往往容易聚集形成包涵体。本文对重组TRAIL包涵体在胞内重折叠转化成可溶性TRAIL蛋白作了初步探索,结果表明：当蛋白表达后,迅速降低温度至30℃并添加50μg／mL氯霉素继续培养4h,可溶性TRAIL产量可提高至16．7％。这一结果在3．7L罐上也得到了证实,可溶性TRAIL表达量达到14．5％。     

Single pH buffer refolding screen for protein from inclusion bodies

We previously reported the set up of an automated test for screening the refolding of recombinant proteins expressed as inclusion bodies in Escherichia coli[1]. The screen used 96 refolding buffers and was validated with 24 proteins, 70% of which remained soluble in at least one buffer. In the present paper, we have analyzed in more detail these experimental data to see if the refolding process can be driven by general rules. Notably, we found that proteins with an acidic isoelectric point (pI) refolded in buffers the average pH of which was alkaline and conversely. In addition, the number of refolding buffers wherein a protein remained soluble increased with the difference between its pI and the average pH of the buffers in which it refolded. A trend analysis of the other variables (ionic strength, detergents, etc.) was also performed. On the basis of this analysis, we devised and validated a new refolding screen made of a single buffer for acidic proteins and a single buffer for alkaline proteins.     

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.     

Ester hydrolyses in reversed micelles using lipase

Lipases are enzymes which require a favourable reaction system for efficient catalysis of their hydrophobic substrates and reversed micellar environment is one such medium which offers many advantages. Hydrolytic studies of esters of paranitrophenol and glycerol using imidazole and four fungal lipases are studied in AOT/isooctane reversed micelles. The effect of water and surfactant concentration on the hydrolysis of rice bran oil is investigated and the overall potential of the reversed micellar system for hydrolytic reactions is assessed.     

Estimating the potential refolding yield of recombinant proteins expressed as inclusion bodies

Recombinant protein production in bacteria is efficient except that insoluble inclusion bodies form when some gene sequences are expressed. Such proteins must undergo renaturation, which is an inefficient process due to protein aggregation on dilution from concentrated denaturant. In this study, the protein-protein interactions of eight distinct inclusion-body proteins are quantified, in different solution conditions, by measurement of protein second virial coefficients (SVCs). Protein solubility is shown to decrease as the SVC is reduced (i.e., as protein interactions become more attractive). Plots of SVC versus denaturant concentration demonstrate two clear groupings of proteins: a more aggregative group and a group having higher SVC and better solubility. A correlation of the measured SVC with protein molecular weight and hydropathicity, that is able to predict which group each of the eight proteins falls into, is presented. The inclusion of additives known to inhibit aggregation during renaturation improves solubility and increases the SVC of both protein groups. Furthermore, an estimate of maximum refolding yield (or solubility) using high-performance liquid chromatography was obtained for each protein tested, under different environmental conditions, enabling a relationship between "yield" and SVC to be demonstrated. Combined, the results enable an approximate estimation of the maximum refolding yield that is attainable for each of the eight proteins examined, under a selected chemical environment. Although the correlations must be tested with a far larger set of protein sequences, this work represents a significant move beyond empirical approaches for optimizing renaturation conditions. The approach moves toward the ideal of predicting maximum refolding yield using simple bioinformatic metrics that can be estimated from the gene sequence. Such a capability could potentially "screen," in silico, those sequences suitable for expression in bacteria from those that must be expressed in more complex hosts.     

Rapid refolding and polishing of single-chain antibodies from Escherichia coli inclusion bodies

An inexpensive and fast-folding strategy for single-chain antibody (scFv) recovered from Escherichia coli inclusion bodies has been developed. Two anti-fluorescein single-chain antibodies, 4-4-20 and 4M5.3, were expressed as inclusion bodies in E. coli for use in a comparative refolding study. Active protein yields as well as degree of aggregation were evaluated for scFv produced by stepwise dialysis, redox dialysis, and a newly developed controlled dilution and filtration strategy. Although all three methods produced active protein for both 4-4-20 and 4M5.3, the extent of aggregation differed greatly among the methods. For 4-4-20, the controlled dilution and filtration strategy reduced aggregation by half, allowed batch processing times of 8h (an 18-fold improvement), and significantly reduced denaturant usage while increasing active yields by 150%. A hydroxyapatite resin polishing step was used to remove completely the aggregate species and inactive monomeric scFv from active scFv.     

Purification of Chromobacterium viscosum lipases using reversed micelles

Summary Two upases produced by Chromobacterium viscosum were isolated and purified by liquid-liquid extraction using organic solvents containing reversed micelles. One lipase (lipase A) was purified from the original crude enzyme preparation by 4,3-fold with a recovery of 91% and the other (lipase B) by 3,7-fold with a recovery of 76%.     

On-column refolding of recombinant human interferon-gamma inclusion bodies by expanded bed adsorption chromatography

A refolding strategy was described for on-column refolding of recombinant human interferon-gamma (rhIFN-gamma) inclusion bodies by expanded bed adsorption (EBA) chromatography. After the denatured rhIFN-gamma protein bound onto the cation exchanger of STREAMLINE SP, the refolding process was performed in expanded bed by gradually decreasing the concentration of urea in the buffer and the refolded rhIFN-gamma protein was recovered by the elution in packed bed mode. It was demonstrated that the denatured rhIFN-gamma protein could be efficiently refolded by this method with high yield. Under appropriate experimental conditions, the protein yield and specific activity of rhIFN-gamma was up to 52.7% and 8.18 x 10(6) IU/mg, respectively.     

Large scale purification and refolding of HIV-1 protease fromEscherichia coli inclusion bodies

The protease encoded by the human immunodeficiency virus type 1 (HIV-1) was engineered inEscherichia coli as a construct in which the natural 99-residue polypeptide was preceded by an NH₂-terminal methionine initiator. Inclusion bodies harboring the recombinant HIV-I protease were dissolved in 50% acetic acid and the solution was subjected to gel filtration on a column of Sephadex G-75. The protein, eluted in the second of two peaks, migrated in SDS-PAGE as a single sharp band ofM _r ≈ 10,000. The purified HIV-1 protease was refolded into an active enzyme by diluting a solution of the protein in 50% acetic acid with 25 volumes of buffer atpH 5.5. This method of purification, which has also been applied to the purification of HIV-2 protease, provides a single-step procedure to produce 100 mg quantities of fully active enzyme.     

Intensified process for the purification of an enzyme from inclusion bodies using integrated expanded bed adsorption and refolding

This work describes the integration of expanded bed adsorption (EBA) and adsorptive protein refolding operations in an intensified process used to recover purified and biologically active proteins from inclusion bodies expressed in E. coli. Delta(5)-3-Ketosteroid isomerase with a C-terminal hexahistidine tag was expressed as inclusion bodies in the cytoplasm of E. coli. Chemical extraction was used to disrupt the host cells and simultaneously solubilize the inclusion bodies, after which EBA utilizing immobilized metal affinity interactions was used to purify the polyhistidine-tagged protein. Adsorptive refolding was then initiated in the column by changing the denaturant concentration in the feed stream from 8 to 0 M urea. Three strategies were tested for performing the refolding step in the EBA column: (i) the denaturant was removed using a step change in feed-buffer composition, (ii) the denaturant was gradually removed using a gradient change in feed-buffer composition, and (iii) the liquid flow direction through the column was reversed and adsorptive refolding performed in the packed bed. Buoyancy-induced mixing disrupted the operation of the expanded bed when adsorptive refolding was performed using either a step change or a rapid gradient change in feed-buffer composition. A shallow gradient reduction in denaturant concentration of the feed stream over 30 min maintained the stability of the expanded bed during adsorptive refolding. In a separate experiment, buoyancy-induced mixing was completely avoided by performing refolding in a settled bed, which achieved comparable yields to refolding in an expanded bed but required a slightly more complex process. A total of 10% of the available KSI-(His(6)) was recovered as biologically active and purified protein using the described purification and refolding process, and the yield was further increased to 19% by performing a second iteration of the on-column refolding operation. This process should be applicable for other polyhistidine tagged proteins and is likely to have the greatest benefit for proteins that tend to aggregate when refolded by dilution.     

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.