Pressure-induced unfolding/refolding of ribonuclease A: static and kinetic Fourier transform infrared spectroscopy study

In this paper, we illustrate the use of high-pressure Fourier transform infrared (FT-IR) spectroscopy to study the reversible presssure-induced unfolding and refolding of ribonuclease A (RNase A) and compare it with the results obtained for the temperature-induced transition. FT-IR spectroscopy monitors changes in the secondary structural properties (amide I' band) or tertiary contacts (tyrosine band) of the protein upon pressurization or depressurization. Analysis of the amide I' spectral components reveals that the pressure-induced denaturation process sets in at 5. 5 kbar at 20 degrees C and pH 2.5. It is accompanied by an increase in disordered structures while the content of beta-sheets and alpha-helices drastically decreases. The denatured state above 7 kbar retains nonetheless some degree of beta-like secondary structure and the molecule cannot be described as an extended random coil. Increase of pH from 2.5 to 5.5 has no influence on the structure of the pressure-denatured state; it slightly changes the stability of the protein only. All experimental evidence indicates that the pressure-denatured states of monomeric proteins have more secondary structure than the temperature-denatured states. Different modes of denaturation, including pressure, may correlate differently with the roughness of the energy scale and slope of the folding funnel. For these reasons we have also carried out pressure-jump kinetic studies of the secondary structural evolution in the unfolding/refolding reaction of RNase A. In agreement with the theoretical model presented by Hummer et al. [(1998) Proc. Natl. Acad. Sci. U.S.A. 95, 1552-1555], the experimental data show that pressure slows down folding and unfolding kinetics (here 1-2 orders of magnitude), corresponding to an increasingly rough landscape. The kinetics remains non-two-state under pressure. Assuming a two-step folding scenario, the calculated relaxation times for unfolding of RNase A at 20 degrees C and pH 2.5 can be estimated to be tau(1) approximately 0.7 min and tau(2) approximately 17 min. The refolding process is considerably faster (tau(1) approximately 0.3 min, tau(2) approximately 4 min). Our data show that the pressure stability and pressure-induced unfolding/refolding kinetics of monomeric proteins, such as wild-type staphylococcal nuclease (WT SNase) and RNase A, may be significantly different. The differences are largely due to the four disulfide bonds in RNase A, which stabilize adjacent structures. They probably lead to the much higher denaturation pressure compared to SNase, and this might also explain why the volume change of WT SNase upon unfolding is about twice as large.     

Protein refolding using chemical refolding additives

In laboratories and manufacturing settings, a rapid and inexpensive method for the preparation of a target protein is crucial for promoting resesrach in protein science and engineering. Inclusion-body-based protein production is a promising method because high yields are achieved in the upstream process, although the refolding of solubilized, unfolded proteins in downstream processes often leads to significantly lower yields. The most challenging problem is that the effective condition for refolding is protein dependent and is therefore difficult to select in a rational manner. Accordingly, considerable time and expense using trial-and-error approaches are often needed to increase the final protein yield. Furthermore, for certain target proteins, finding suitable conditions to achieve an adequate yield cannot be obtained by existing methods. Therefore, to convert such a troublesome refolding process into a routine one, a wide array of methods based on novel technologies and materials have been developed. These methods select refolding conditions where productive refolding dominates over unproductive aggregation in competitive refolding reactions. This review focuses on synthetic refolding additives and describes the concepts underlying the development of reported chemical additives or chemical-additive-b     

Modeling and simulation of fed-batch protein refolding process

The simplified kinetic model that assumes competition between first-order folding and third-order aggregation was used to model the fed-batch refolding of denatured-reduced lysozyme. It was found that the model was able to describe the process at limited concentration ranges, i.e., 1-2 and 5-7 mg mL(-)(1), respectively, at extensive guanidinium chloride (GdmCl) concentrations and controlled concentrations of oxidizing and reducing agents. The folding or aggregation rate constant was different at the two protein concentration ranges and strongly dependent on the denaturant concentration. As a result, both rate constants at the two concentration ranges were expressed as functions of GdmCl concentration. The rate constants determined by fed-batch experiments could be employed for the prediction of the fed-batch process but were not able to be extended to a batch refolding by direct dilution. Computer simulations show that the denaturant concentration and fed-batch flow rate are important factors influencing the refolding yield. Prolonged fed-batch time is beneficial to keep the transient intermediate concentration at a low level and to increase the yield of correctly folded protein. This is of importance when the denaturant concentration in refolding buffer solution is low. Thus, at a low denaturant concentration, fed-batch time should be sufficiently long, whereas at an appropriately high GdmCl concentration, a short fed-batch time or a high feed rate of the denatured protein is effective to give a high refolding yield.     

Technical refolding of proteins: Do we have freedom to operate?

Expression as inclusion bodies in Escherichia coli is a widely used method for the large-scale production of therapeutic proteins that do not require post-translational modifications. High expression yields and simple recovery steps of inclusion bodies from the host cells are attractive features industrially. However, the value of an inclusion body-based process is dominated by the solubilization and refolding technologies. Scale-invariant technologies that are economical and applicable for a wide range of proteins are requested by industry. The main challenge is to convert the denatured protein into its native conformation at high yields. Refolding competes with misfolding and aggregation. Thus, the yield of native monomer depends strongly on the initial protein concentrations in the refolding solution. Reasonable yields are attained at low concentrations (≤0.1 mg/mL). However, large buffer tanks and time-consuming concentration steps are required. We attempt to answer the question of the extent to which refolding of proteins is protected by patents. Low-molecular mass additives have been developed to improve refolding yields through the stabilization of the protein in solution and shielding hydrophobic patches. Progress has been made in the field of high-pressure renaturation and on-column refolding. Mixing times of the denatured protein in the refolding buffer have been reduced using newly developed devices and the introduction of specific mixers. Concepts of continuous refolding have been introduced to reduce tank sizes and increase yields. Some of the patents covering refolding of proteins will soon expire or have already expired. This gives more freedom to operate.     

Improving the refolding of NTA protein by urea gradient and arginine gradient size-exclusion chromatography

Inclusion body refolding processes play a major role in the production of recombinant proteins. Improvement of the size-exclusion chromatography refolding process was achieved by combining a decreasing urea gradient with an increasing arginine gradient (two gradients) for the refolding of NTA protein (a new thrombolytic agent) in this paper. Different refolding methods and different operating conditions in two gradients gel filtration process were investigated with regard to increasing the NTA protein activity recovery and inhibition of aggregation. The refolding of denatured NTA protein showed this method could significantly increase the activity recovery of protein at high protein concentration. The activity recovery of 37% was obtained from the initial NTA protein concentration up to 20 mg/ml. The conclusions presented in this study could also be applied to the refolding of lysozyme.     

Capture of monomeric refolding intermediate of human muscle creatine kinase

Human muscle creatine kinase (CK) is an enzyme that plays an important physiological role in the energy metabolism of humans. It also serves as a typical model for studying refolding of proteins. A study of the refolding and reactivation process of guanidine chloride-denatured human muscle CK is described in the present article. The results show that the refolding process can be divided into fast and slow folding phases and that an aggregation process competes with the proper refolding process at high enzyme concentration and high temperature. An intermediate in the early stage of refolding was captured by specific protein molecules: the molecular chaperonin GroEL and alpha(s)-casein. This intermediate was found to be a monomer, which resembles the "molten globule" state in the CK folding pathway. To our knowledge, this is the first monomeric intermediate captured during refolding of CK. We propose that aggregation is caused by interaction between such monomeric intermediates. Binding of GroEL with this intermediate prevents formation of aggregates by decreasing the concentration of free monomeric intermediates, whereas binding of alpha(s)-casein with this intermediate induces more aggregation.     

The effect of temperature on protein refolding at high pressure: Enhanced green fluorescent protein as a model

The application of high hydrostatic pressure (HHP) impairs electrostatic and hydrophobic intermolecular interactions, promoting the dissociation of recombinant inclusion bodies (IBs) under mild conditions that favor subsequent protein refolding. We demonstrated that IBs of a mutant version of green fluorescent protein (eGFP F64L/S65T), produced at 37 °C, present native-like secondary and tertiary structures that are progressively lost with an increase in bacterial cultivation temperature. The IBs produced at 37 °C are more efficiently dissociated at 2.4 kbar than those produced at 47 °C, yielding 25 times more soluble, functional eGFP after the lower pressure (0.69 kbar) refolding step. The association of a negative temperature (−9 °C) with HHP enhances the efficiency of solubilization of IBs and of eGFP refolding. The rate of refolding of eGFP as temperature increases from 10 °C to 50 °C is proportional to the temperature, and a higher yield was obtained at 20 °C. High level refolding yield (92%) was obtained by adjusting the temperatures of expression of IBs (37 °C), of their dissociation at HHP (−9 °C) and of eGFP refolding (20 °C). Our data highlight new prospects for the refolding of proteins, a process of fundamental interest in modern biotechnology.     

Process analytical technology implementation for protein refolding: GCSF as a case study

Process analytical technology is gaining interest in the biopharmaceutical industry as a means to enable consistency in processing and thereby in product quality via process control. Protein refolding is known to be significantly impacted by critical process parameters and feed material attributes including composition and pH of the solubilisation and refolding buffers. Hence, to achieve robust process control and product quality, these attributes and parameters need to be monitored. This paper presents an approach towards statistical process control and monitoring of protein refolding, from buffer preparation to refold quenching, during manufacturing of therapeutic proteins from Escherichia coli based systems. The proposed approach utilises measurements of online redox potential, temperature, and pH for development of a statistical model. The model has then been integrated with LabView to permit real-time monitoring of the refolding process. The proposed system has been demonstrated to successfully identify process deviations and thereby enable process control for manufacturing product of consistent quality.     

Non-chromatographic strategies for protein refolding

Overexpression of recombinant proteins in bacterial systems (such as E. coli) often leads to formation of inactive and insoluble ' inclusion bodies' . Protein refolding refers to folding back the proteins after solubilizing/unfolding the misfolded proteins of the inclusion bodies. Protein aggregation, a concentration dependent phenomenon, competes with refolding pathway. The refolding strategies largely aim at reducing aggregation and/or promoting correct folding. This review focuses on non-chromatographic strategies for refolding like dilution, precipitation, three phase partitioning and macro-(affinity ligand) facilitated three phase partitioning. The nanomaterials which disperse well in aqueous buffers are also discussed in the context of facilitating protein refolding. Apart from general results with these methods, the review also covers the use of non-chromatographic methods in protein refolding in the patented literature beyond 2000. The patented literature generally describes use of cocktail of additives which results in increase in refolding yield. Such additives include low concentration of chaotropic agents, redox systems, ions like SO4(2-) and Cl-, amines, carboxylic acids and surfactants. Some novel approaches like use of a "pressure window" or ionic liquids for refolding and immobilized diselenide compounds for ensuring correct -S-S- bonds pairing have also been discussed in various patents. In most of the patented literature, focus naturally has been on refolding in case of pharmaceutical proteins.     

Preparative protein refolding

The rapid provision of purified native protein underpins both structural biology and the development of new biopharmaceuticals. The dominance of Escherichia coli as a cellular biofactory depends on technology for solubilizing and refolding proteins that are expressed as insoluble inclusion bodies. Such technology must be scale invariant, easily automated, generic for a broad range of similar proteins and economical. Refolding methods relying on denaturant dilution and column-based approaches meet these criteria. Recent developments, particularly in column-based methods, promise to extend the range of proteins that can be refolded successfully. Developments in preparing denatured purified protein and in the analysis of protein refolding products promise to remove bottlenecks in the overall process. Combined, these developments promise to facilitate the rapid and automated determination of appropriate refolding conditions and to simplify scale-up.     

Factors affecting protein refolding yields in a fed-batch and batch-refolding system

The refolding of recombinant protein from inclusion bodies expressed in Escherichia coli can present a process bottleneck. Yields at industrially relevant concentrations are restricted by aggregation of protein upon dilution of the denatured form. This article studies the effect of five factors upon the dilution refolding of protein in a twin impeller fed-batch system using refold buffer containing only the oxidized form of the redox reagent. Such a buffer is easier to prepare and more stable than a buffer containing both reduced and oxidized forms. The five factors chosen were: bulk impeller Reynolds number, mini-impeller Reynolds number, injection rate of denatured protein, redox ratio, and guanidine hydrochloride (GdHCl) concentration. A 2(5) factorial experiment was conducted at an industrially relevant protein concentration using lysozyme as the test system. The study identified that in the system used, the guanidine hydrochloride concentration, redox ratio, and injection rate were the most important factors in determining refolding yields. Two interactions were found to be important: redox ratio/guanidine hydrochloride concentration and guanidine hydrochloride concentration/injection rate. Conditions were also found at which high refolding yields could be achieved even with rapid injection and poor mixing efficiency. Therefore, a comparative assessment was carried out with minimal mixing in a simple batch-refolding mode of operation, which revealed different behavior to that of fed-batch. A graphical (windows of operation) analysis of the batch data suggested that optimal yields and productivity are obtained at high guanidine hydrochloride concentrations (1.2 M) and redox ratios of unity or greater.     

Current status of technical protein refolding

The expression of heterologous proteins in microbial hosts frequently leads to the formation of insoluble aggregates. To fully exploit the production capacity of the cells, efficient strategies for further processing have to be developed. While in lab scale matrix assisted refolding techniques, especially of histidine-tagged proteins have become very popular, in production scale refolding by dilution is still predominant due to its simplicity. However scaling up dilution processes leads to large volumes and low protein concentration. This is a heavy burden both for liquid handling and for subsequent downstream processing steps. Process development aims to operate at uniform, reproducible conditions, to reduce costs to a minimum and to guarantee the required quality of the product. The general refolding kinetics, exploration of appropriate refolding conditions are reviewed. The major refolding operations such as dilution, matrix assisted refolding, pressure driven refolding or continuous refolding applications are discussed in view of industrial applicability.     

High-pressure refolding of bikunin: efficacy and thermodynamics

Bikunin is a glycosylated protein that aggregates extensively during mammalian cell culture, resulting in loss of activity, loss of native secondary structure, and the formation of nonnative disulfide bonds. We investigated the use of high hydrostatic pressure (1000-3000 bar) for the refolding of bikunin aggregates. The refolding yield obtained with pressure-modulated refolding at 2000 bar was 70 (+/-5%) by reverse-phase chromatography (RP-HPLC), significantly higher than the value of 55 (+/-6%) (RP-HPLC) obtained with traditional guanidine HCl "dilution-refolding." In addition, we determined the thermodynamics of pressure-modulated refolding. The change in volume for the transition of aggregate to monomer DeltaV(refolding) was calculated to be -28 (+/-5) mL/mole. Refolding was accompanied by a loss of hydrophobic exposure, resulting in a positive contribution to the DeltaV(refolding). These findings suggest that the disruption of electro-static interactions or the differences in size of solvent-free cavities between the aggregate and the monomer are the prevailing contributions to the negative DeltaV(refolding).     

High productivity refolding of an inclusion body protein using pulsed-fed size exclusion chromatography

Protein refolding using size exclusion chromatography (SEC) is advantageous over conventional refolding methods in terms of ease of automation, simultaneous purification capabilities, and the non-adsorptive protein–matrix interaction which eliminates steric constraints. Despite these advantages, the widespread use of SEC refolding remains restricted by low process productivity and product concentration bottlenecks. This study aims to address those limitations and exploit SEC advantages for large-scale refolding applications. Specifically, this study reports the development of a pulsed-fed size exclusion chromatography (PF-SEC) refolding platform, which successfully refolded E. coli-derived α-fetoprotein (AFP) to achieve 53% refolding yield at 0.9 mg/ml AFP refolding concentration. AFP was introduced into the column by pulsed injection to increase feed load, while suppressing concentration-induced aggregation. Refolding was initiated by a urea gradient in the column, where the gradient length could be readily adjusted to complement pulsed feeding patterns. AFP refolding productivity with PF-SEC improved by 8- and 64-fold compared to ion-exchange chromatography refolding and pulsed dilution refolding, respectively, at a fixed refolding concentration. Through a unique integration of pulsed feeding and urea gradient development, this new PF-SEC refolding methodology overcomes ‘productivity and concentration’-related disadvantages inherent in SEC, and will be scalable for large-scale protein refolding applications.     

Operational regimes for a simplified one-step artificial chaperone refolding method

The "artificial chaperone method" for protein refolding developed by Rozema et al. (Rozema, D.; Gellman, S. H. J. Am. Chem. Soc. 1995, 117 (8), 2373-2374) involves the sequential dilution of denatured protein into a buffer containing detergent (cetyltrimethylammonium bromide, CTAB) and then into a refolding buffer containing cyclodextrin (CD). In this paper a simplified one-step artificial chaperone method is reported, whereby CTAB is added directly to the denatured solution, which is then diluted directly into a refolding buffer containing beta-cyclodextrin (beta-CD). This new method can be applied at high protein concentrations, resulting in smaller processing volumes and a more concentrated protein solution following refolding. The increase in achievable protein concentration results from the enhanced solubility of CTAB at elevated temperatures in concentrated denaturant. The refolding yields obtained for the new method were significantly higher than for control experiments lacking additives and were comparable to the yields obtained with the classical two-step approach. A study of the effect of beta-CD and CTAB concentrations on refolding yield suggested two operational regimes: slow stripping (beta-CD/CTAB approximately 1), most suited for higher protein concentrations, and fast stripping (beta-CD/CTAB approximately 2.7), best suited for lower protein concentrations. An increased chaotrope concentration resulted in higher refolding yields and an enlarged operational regime.     

Antiperoxidase antibodies enhance refolding of horseradish peroxidase

The effect of monoclonal antibodies on protein folding was studied using horseradish peroxidase refolding from guanidine hydrochloride as a model process. Among the five antiperoxidase clones tested, one was found to increase the yield of catalytically active peroxidase after guanidine treatment. The same clone also increased the activity of the native peroxidase by a factor of 2-2.5. While peroxidase refolding under standard conditions resulted in the recovery of only 7-8% of the initial catalytic activity, antibody-assisted refolding increased the yield to 50-100% (or 20-40% from the activity of native enzyme with antibodies). Kinetics of autorefolding and antibody-assisted refolding differed significantly. In the course of autorefolding the catalytic activity was recovered within the first 2.5 min and did not change further within a 2.5- to 60-min interval, whereas in the course of antibody-assisted refolding maximal catalytic activity was attained only in 60 min. The yield of active peroxidase for the antibody-assisted refolding depended linearly on the antibody concentration. The observed effect was strongly specific. Other antiperoxidase clones tested as well as nonspecific antithyroglobulin antibody affected neither kinetics, no the yield of peroxidase refolding.     

Confronting high-throughput protein refolding using high pressure and solution screens

Over-expression of heterologous proteins in Escherichia coli is commonly hindered by the formation of inclusion bodies. Nevertheless, refolding of proteins in vitro has become an essential requirement in the development of structural genomics (proteomics) and as a means of recovering functional proteins from inclusion bodies. Many distinct methods for protein refolding are now in use. However, regardless of method used, developing a reliable protein refolding protocol still requires significant optimization through trial and error. Many proteins fall into the category of "Challenging" or "Difficult to Express" and are problematic to refold using traditional chaotrope-based refolding techniques. This review discusses new methods for improving protein refolding, such as implementing high hydrostatic pressure, using small molecule additives to enhance traditional protein refolding strategies, as well as developing practical methods for performing refolding studies to maximize their reliability and utility. The strategies examined here focus on high-throughput, automated refolding screens, which can be applied to structural genomic projects.     

High recovery refolding of rhG-CSF from Escherichia coli, using urea gradient size exclusion chromatography

Protein folding liquid chromatography (PFLC) is a powerful tool for simultaneous refolding and purification of recombinant proteins in inclusion bodies. Urea gradient size exclusion chromatography (SEC) is a recently developed protein refolding method based on the SEC refolding principle. In the presented work, recombinant human granulocyte colony-stimulating factor (rhG-CSF) expressed in Escheriachia coli (E. coli) in the form of inclusion bodies was refolded with high yields by this method. Denatured/reduced rhG-CSF in 8.0 mol.L(-1) urea was directly injected into a Superdex 75 column, and with the running of the linear urea concentration program, urea concentration in the mobile phase and around the denatured rhG-CSF molecules was decreased linearly, and the denatured rhG-CSF was gradually refolded into its native state. Aggregates were greatly suppressed and rhG-CSF was also partially purified during the refolding process. Effects of the length and the final urea concentration of the urea gradient on the refolding yield of rhG-CSF by using urea gradient SEC were investigated respectively. Compared with dilution refolding and normal SEC with a fixed urea concentration in the mobile phase, urea gradient SEC was more efficient for rhG-CSF refolding--in terms of specific bioactivity and mass recovery, the denatured rhG-CSF could be refolded at a larger loading volume, and the aggregates could be suppressed more efficiently. When 500 microL of solubilized and denatured rhG-CSF in 8.0 mol.L(-1) urea solution with a total protein concentration of 2.3 mg.mL(-1) was loaded onto the SEC column, rhG-CSF with a specific bioactivity of 1.0 x 10(8) IU.mg(-1) was obtained, and the mass recovery was 46.1%.     

Refolding of proteins from inclusion bodies is favored by a diminished hydrophobic effect at elevated pressures

The application of high hydrostatic pressure is an effective tool to promote dissolution and refolding of protein from aggregates and inclusion bodies while minimizing reaggregation. In this study we explored the mechanism of high-pressure protein refolding by quantitatively assessing the magnitude of the protein-protein interactions both at atmospheric and elevated pressures for T4 lysozyme, in solutions containing various amounts of guanidinium hydrochloride. At atmospheric pressure, the protein- protein interactions are most attractive at moderate guanidinium hydrochloride concentrations (approximately 1-2 molar), as indicated by a minimum in B(22) values. In contrast, at a pressure of 1,000 bar no minimum in B(22) values is observed, indicating that high pressures colloidally stabilize protein against aggregation. Finally, experimental values of refractive index increments as a function of pressure indicate that at high pressures, wetting of the hydrophobic surfaces is favored, resulting in a reduction of the hydrophobic effect. This reduction in the hydrophobic effect reduces the driving force for aggregation of (partially) unfolded protein.     

Intermediate studies on refolding of arginine kinase denatured by guanidine hydrochloride.

The refolding course and intermediate of guanidine hydrochloride (GuHCl)-denatured arginine kinase (AK) were studied in terms of enzymatic activity, intrinsic fluorescence, 1-anilino-8-naphthalenesulfonte (ANS) fluorescence, and far-UV circular dichroism (CD). During AK refolding, the fluorescence intensity increased with a significantly blue shift of the emission maximum. The molar ellipticity of CD increased to close to that of native AK, as compared with the fully unfolded AK. In the AK refolding process, 2 refolding intermediates were observed at the concentration ranges of 0.8-1.0 mol/L and 0.3-0.5 mol GuHCl/L. The peak position of the fluorescence emission and the secondary structure of these conformation states remained roughly unchanged. The tryptophan fluorescence intensity increased a little. However, the ANS fluorescence intensity significantly increased, as compared with both the native and the fully unfolded states. The first refolding intermediate at the range of 0.8-1.0 mol GuHCl/L concentration represented a typical "pre-molten globule state structure" with inactivity. The second one, at the range of 0.3-0.5 mol GuHCl/L concentration, shared many structural characteristics of native AK, including its secondary and tertiary structure, and regained its catalytic function, although its activity was lower than that of native AK. The present results suggest that during the refolding of GuHCl-denatured AK there are at least 2 refolding intermediates; as well, the results provide direct evidence for the hierarchical mechanism of protein folding.