Continuous matrix assisted refolding of alpha-lactalbumin by ion exchange chromatography with recycling of aggregates combined with ultradiafiltration

Continuous matrix assisted refolding (MAR) can be achieved on a solid support by using a continuous chromatographic system. Recycling the aggregate fraction, simultaneously formed during a refolding reaction, can further increase the refolding yield. Due to the nature of this reaction, aggregates are the main reason for a refolding yield below stoichiometric conversion. A preparative continuous annular chromatographic system (P-CAC) equipped with an ion exchange resin was used to continuously refold the model protein alpha-lactalbumin. For this purpose, this protein was denatured, reduced and adsorbed on the ion exchange resin. Elution was performed with or without redox reagents in the buffer system permitting fast formation of the native disulfide bonds. In the case redox reagents were present, the protein refolds then during its residence time on the matrix. However, aggregate formation is also increased and refolding yields are lower. Tightly bound aggregates were removed from the column by 2M guanidinium hydrochloride. In order to increase the system yield, this aggregate fraction was recycled after lowering the conductivity by ultradiafiltration and adjustment of the protein concentration by dilution. For on-column refolding, recycling of aggregates at a recycling rate of 0.17 increased the system yield from 25% to 30%. An algorithm was developed to show interdependencies of the single influencing parameters. The operability of the system was demonstrated but limitations due to instability of the P-CAC, especially inhomogeneous flow and peak wobbling, have to be considered.     

One‐step refolding and purification of recombinant human tumor necrosis factor‐α (rhTNF‐α) using ion‐exchange chromatography

Protein refolding is a key step for the production of recombinant proteins, especially at large scales, and usually their yields are very low. Chromatographic‐based protein refolding techniques have proven to be superior to conventional dilution refolding methods. High refolding yield can be achieved using these methods compared with dilution refolding of proteins. In this work, recombinant human tumor necrosis factor‐α (rhTNF‐α) from inclusion bodies expressed in Escherichia coli was renatured with simultaneous purification by ion exchange chromatography with a DEAE Sepharose FF column. Several chromatographic parameters influencing the refolding yield of the denatured/reduced rhTNF‐α, such as the urea concentration, pH value and concentration ratio of glutathione/oxidized glutathione in the mobile phase, were investigated in detail. Under optimal conditions, rhTNF‐α can be renatured and purified simultaneously within 30 min by one step. Specific bioactivity of 2.18 × 10⁸ IU/mg, purity of 95.2% and mass recovery of 76.8% of refolded rhTNF‐α were achieved. Compared with the usual dilution method, the ion exchange chromatography method developed here is simple and more effective for rhTNF‐α refolding in terms of specific bioactivity and mass recovery. Copyright © 2014 John Wiley & Sons, Ltd.     

Renaturation with simultaneous purification of rhG-CSF from Escherichia coli by ion exchange chromatography

Protein refolding is a key step for the production of recombinant proteins, especially at large scales, and usually their yields are very low. Application of liquid chromatography to protein refolding is an exciting step forward for this field. In this work, recombinant human granulocyte colony-stimulating factor (rhG-CSF) expressed in Escherichia coli was renatured with simultaneous purification by ion exchange chromatography (IEC) with a Q Sepharose FF column. Several chromatographic parameters affecting the refolding yield of the denatured/reduced rhG-CSF, such as the urea concentration, pH value, concentration and ratio of reduced/oxidized glutathione in the mobile phase, as well as the flow rate of the mobile phase, were investigated in detail and indicated that the urea concentration and the pH value were of great importance. At the optimal conditions, the renatured and purified rhG-CSF was found to have a specific bioactivity of 3.0 x 10(8) IU/mg, a purity of 96%, and a mass recovery of 49%. Compared with the usual dilution method, the IEC method developed here is more effective for rhG-CSF refolding in terms of specific bioactivity and mass recovery.     

Matrix-assisted refolding of autoprotease fusion proteins on an ion exchange column

Refolding of proteins must be performed under very dilute conditions to overcome the competing aggregation reaction, which has a high reaction order. Refolding on a chromatography column partially prevents formation of the intermediate form prone to aggregation. A chromatographic refolding procedure was developed using an autoprotease fusion protein with the mutant EDDIE from the N^pro autoprotease of pestivirus. Upon refolding, self-cleavage generates a target peptide with an authentic N-terminus. The refolding process was developed using the basic 1.8-kDa peptide sSNEVi-C fused to the autoprotease EDDIE or the acidic peptide pep6His, applying cation and anion exchange chromatography, respectively. Dissolved inclusion bodies were loaded on cation exchange chromatographic resins (Capto S, POROS HS, Fractogel EMD SO₃⁻, UNOsphere S, SP Sepharose FF, CM Sepharose FF, S Ceramic HyperD F, Toyopearl SP-650, and Toyopearl MegaCap II SP-550EC). A conditioning step was introduced in order to reduce the urea concentration prior to the refolding step. Refolding was initiated by applying an elution buffer containing a high concentration of Tris–HCl plus common refolding additives. The actual refolding process occurred concurrently with the elution step and was completed in the collected fraction. With Capto S, POROS HS, and Fractogel SO₃⁻, refolding could be performed at column loadings of 50 mg fusion protein/ml gel, resulting in a final eluate concentration of around 10–15 mg/ml, with refolding and cleavage step yields of around 75%. The overall yield of recovered peptide reached 50%. Similar yields were obtained using the anion exchange system and the pep6His fusion peptide. This chromatographic refolding process allows processing of fusion peptides at a concentration range 10- to 100-fold higher than that observed for common refolding systems.     

Refolding and simultaneous purification of recombinant human proinsulin from inclusion bodies on protein‐folding liquid‐chromatography columns

Protein‐folding liquid chromatography (PFLC) is an effective and scalable method for protein renaturation with simultaneous purification. However, it has been a challenge to fully refold inclusion bodies in a PFLC column. In this work, refolding with simultaneous purification of recombinant human proinsulin (rhPI) from inclusion bodies from Escherichia coli were investigated using the surface of stationary phases in immobilized metal ion affinity chromatography (IMAC) and high‐performance size‐exclusion chromatography (HPSEC). The results indicated that both the ligand structure on the surface of the stationary phase and the composition of the mobile phase (elution buffer) influenced refolding of rhPI. Under optimized chromatographic conditions, the mass recoveries of IMAC column and HPSEC column were 77.8 and 56.8% with purifies of 97.6 and 93.7%, respectively. These results also indicated that the IMAC column fails to refold rhPI, and the HPSEC column enables efficient refolding of rhPI with a low‐urea gradient‐elution method. The refolded rhPI was characterized by circular dichroism spectroscopy. The molecular weight of the converted human insulin was further confirmed with SDS–18% PAGE, Matrix‐Assisted Laser Desorption/ Ionization Time of Flight Mass Spectrometry (MALDI‐TOF‐MS) and the biological activity assay by HP‐RPLC. Copyright © 2014 John Wiley & Sons, Ltd.     

On-line purification of His-tag enhanced green fluorescent protein taken directly from a bioreactor by continuous ultrasonic homogenization coupled with immobilized metal affinity expanded bed adsorption

Protein refolding at high concentrations always leads to aggregation, which limits commercial application. An ion-exchange chromatography process with gradient changes in urea concentration and pH was developed to refold denatured lysozyme at high concentration. After adsorption of the denatured protein onto an ion-exchange medium, elution was carried out in combination with a gentle decrease in urea concentration and elevation of pH. Protein would gradually refold along the column with high activity yield. Denatured and reduced lysozyme at 40 mg/ml was loaded into a column filled with SP Sepharose Fast Flow, resulting in 95% activity recovery and 98% mass yield within a short period of time.     

Purification of a crystallin domain of Yersinia crystallin from inclusion bodies and its comparison to native protein from the soluble fraction

It has been established that many heterologously produced proteins in E. coli accumulate as insoluble inclusion bodies. Methods for protein recovery from inclusion bodies involve solubilization using chemical denaturants such as urea and guanidine hydrochloride, followed by removal of denaturant from the solution to allow the protein to refold. In this work, we applied on-column refolding and purification to the second crystallin domain D2 of Yersinia crystallin isolated from inclusion bodies. We also purified the protein from the soluble fraction (without using any denaturant) to compare the biophysical properties and conformation, although the yield was poor. On-column refolding method allows rapid removal of denaturant and refolding at high protein concentration, which is a limitation in traditionally used methods of dialysis or dilution. We were also able to develop methods to remove the co-eluting nucleic acids during chromatography from the protein preparation. Using this protocol, we were able to rapidly refold and purify the crystallin domain using a two-step process with high yield. We used biophysical techniques to compare the conformation and calcium-binding properties of the protein isolated from the soluble fraction and inclusion bodies.     

Size-exclusion chromatographic protein refolding: fundamentals, modeling and operation

Size-exclusion chromatography (SEC) has proven its capability to refold a variety of proteins using a range of gel filtration column materials, demonstrated in the growing body of experimental evidence. However, little effort has been allocated to the development of mechanistic models describing size-exclusion chromatographic refolding reactors (SECRR). Mechanistic models are important since they provide a link between process variables like denatured and reduced protein feed concentration (C_f,D&;R), flow rate, column length, etc., and performance indicators like refolding yield (Y_N), thereby opening the possibility for in silico design of SECRRs. A critical step, in the formulation of such models, is the selection of an adequate reaction mechanism, which provides the direct link between the separation and the refolding yield. Therefore, in this work we present a methodology using a SEC refolding reactor model, supported by a library of reaction mechanisms, to estimate a suitable reaction scheme using experimental SEC refolding data. SEC refolding data is used since it provides information about the mass distribution of monomers and aggregates after refolding, information not readily available from batch dilution refolding data alone. Additionally, this work presents (1) a systematic analysis of the reaction mechanisms considered using characteristic time analysis and Damköhler maps, revealing (a) the direct effect of a given reaction mechanism on the shape of the SEC refolding chromatogram (number of peaks and resolution) and (b) the effect that the competition between convection, refolding and aggregation is likely to have on the SEC refolding yield; (2) a comparison between the SECR reactor and the batch dilution refolding reactor based on mechanistic modeling, quantitatively showing the advantages of the former over the latter; and (3) the successful application of the modeling based strategy to study the SEC refolding data of an industrially relevant protein. In principle, the presented modeling strategy can be applied to any protein refolded using any gel filtration material, providing the proper mass balances and activity measurements are available.     

Controlled oxidative protein refolding using an ion-exchange column

Column-based refolding of complex and highly disulfide-bonded proteins simplifies protein renaturation at both preparative and process scale by integrating and automating a number of operations commonly used in dilution refolding. Bovine serum albumin (BSA) was used as a model protein for refolding and oxido-shuffling on an ion-exchange column to give a refolding yield of 55% after 40 h incubation. Successful on-column refolding was conducted at protein concentrations of up to 10 mg/ml and refolded protein, purified from misfolded forms, was eluted directly from the column at a concentration of 3 mg/ml. This technique integrates the dithiothreitol removal, refolding, concentration and purification steps, achieving a high level of process simplification and automation, and a significant saving in reagent costs when scaled. Importantly, the current result suggests that it is possible to controllably refold disulfide-bonded proteins using common and inexpensive matrices, and that it is not always necessary to control protein-surface interactions using affinity tags and expensive chromatographic matrices. Moreover, it is possible to strictly control the oxidative refolding environment once denatured protein is bound to the ion-exchange column, thus allowing precisely controlled oxido-shuffling.     

Refolding of detergent‐denatured lysozyme using β‐cyclodextrin‐assisted ion exchange chromatography

Chromatography‐based protein refolding is widely used. Detergent is increasingly used for protein solubilization from inclusion bodies. Therefore, it is necessary to develop a refolding method for detergent‐denatured/solubilized proteins based on liquid chromatography. In the present work, sarkosyl‐denatured/dithiothreitol‐reduced lysozyme was used as a model, and a refolding method based on ion exchange chromatography, assisted by β‐cyclodextrin, was developed for refolding detergent‐denatured proteins. Many factors affecting the refolding, such as concentration of urea, concentration of β‐cyclodextrin, pH and flow rate of mobile phases, were investigated to optimize the refolding conditions for sarkosyl‐denatured lysozymes. The results showed that the sarkosyl‐denatured lysozyme could be successfully refolded using β‐cyclodextrin‐assisted ion exchange chromatography. Copyright © 2012 John Wiley & Sons, Ltd.     

Glycerol-Assisted Hydrophobic Interaction Chromatography Improving Refolding of Recombinant Human Granulocyte Colony-Stimulating Factor

Efficient refolding of recombinant proteins in the forms of inclusion bodies at higher concentration remains challenging. Here, we report a strategy of a dual-gradient hydrophobic interaction chromatography (HIC) mode to refold recombinant human granulocyte colony-stimulating factor from its inclusion bodies at high protein concentration. The strategy was taken to meet the demand of dynamic refolding proceeding by gradually decrease the denaturant (guanidine-HCl) concentration and gradually increase the hydrophilicity of media (column of Poros PE 20) with glycerol as additive to provide a mild refolding surroundings. Compared with dilution method, this dual-gradient HIC process gave about 8.5-fold of increase in specific activity and 30% increase in soluble protein recovery. Furthermore, much higher protein concentration could be obtained at the same time.     

Mechanism of simultaneously refolding and purification of proteins by hydrophobic interaction chromatographic unit and applications

The hydrophobic amino acid residues of a denatured protein molecule tend to react with the particles of the stationary phase of hydrophobic interaction chromatography (STHIC). These hydrophobic interactions prevent the denatured protein molecules from aggregating with each other. The STHIC can provide high enough energy to a denatured protein molecule to make it dehydration and to refold it into its native or various intermediate states. The outcome not only depends on the specific interactions between amino acids, the structure of STHIC, but also depends on the association between the STHIC and mobile phase. The mechanism of protein refolding and the principle of its quality control by HPHIC were also presented. By appropriate selection of the chromatographic condition, several denatured proteins can be refolded and separated simultaneously in a single chromatographic run. A specially designed unit, with diameter much larger than its length, was designed and employed for both laboratory and preparative     

Lysozyme refolding with immobilized GroEL column chromatography

A refolding chromatography with immobilized molecular chaperonin GroEL was studied for the reactivation of denatured-reduced lysozyme. The effect of denaturant concentration (guanidine hydrochloride, 0.1-1.5 M) in the elution buffer, the elution flow-rate, and the loading concentration and volume of the substrate protein on the reactivation yield was studied. All the operating parameters showed minor effects on the recovery yield of lysozyme mass, which remained at 90-100%, but exhibited relatively notable influences on the specific activity of the recovered lysozyme. For example, there existed an optimum denaturant concentration of about 1 M at which the highest yield of specific activity (up to 97%) was obtained. Using the immobilized GroEL column, 3 ml of the lysozyme (1 mg/ml) per batch could be refolded at an overall yield of 81%, which corresponded to a refolding productivity of 54 mg per 1 gel per h. At comparable reactivation yields (over 80%), this value of productivity was over four-times larger as that of the size-exclusion refolding chromatography reported previously (12 mg per 1 gel per h), indicating the advantage of the present system for producing a high throughput in protein refolding operations.     

Novel column-based protein refolding strategy using dye-ligand affinity chromatography based on macroporous biomaterial

A novel column-based chromatographic protein refolding strategy was developed using dye-ligand affinity chromatography (DLAC) based on macroporous biomaterial. Chitosan–silica (CS–silica) biomaterial with macroporous surface was used as the supporting matrix for the preparation of the DLAC material. The dye-ligand Cibacron Blue F3GA (CBF) was selected as affinity handle and could be covalently immobilized to form dye-ligand affinity adsorbent (CBF–CS–silica) using the reactivity of NH₂ on CS–silica biomaterial. After the model protein catalase was denatured with 6 mol/L urea, the denaturant could be rapidly removed and catalase could be successfully refolded as facilitated by the adsorption of CBF–CS–silica. The urea denaturation process and the elute condition for the chromatographic refolding were optimized by measuring tryptophan fluorescence and activity of catalase. The refolding performance of the proposed DLAC was compared with dilution refolding. The protein concentration during the proposed chromatographic refolding increased by a factor of 20 without reducing the yield achieved as compared to dilution refolding. The column-based protein refolding strategy based on dye-ligand affinity chromatography with porous biomaterial being matrix possessed potential in chromatographic refolding of protein.     

Preparation of phenylboronic acid functionalized cation-exchange monolithic columns for protein separation and refolding

In this study, we described a simple and effective modification procedure to prepare poly (methacrylate-co-ethylene glycol dimethacrylate) monolithic columns functionalized with 3-aminophenylboronic acid. The column morphology, pore size and specific surface area of the fabricated monolith were characterized by scanning electron microscopy, X-ray photoelectron spectroscopy, thermogravimetric analysis, and mercury intrusion porosimeter, respectively. The frontal analysis was carried out for dynamic loading capacity of the model protein on the modified column. The chromatographic performance of the cation-exchange monolith was evaluated through separating a mixture of five proteins such as lysozyme, cytochrome c, ribonuclease A, trypsin and bovine serum albumin and one-step purification of lysozyme from egg whites, and the expected results were obtained. In addition, the functionalized column was used to refold ribonuclease A and cytochrome c, and this procedure was monitored by circular dichroism and fluorescence spectroscopy. Compared with the conventional dilution refolding method, the ion-exchange chromatography refolding method developed here is more effective for specific bioactivity recovery.     

Refolding and purification of rhNTA protein by chromatography

RhNTA protein is a new thrombolytic agent which has potential medicinal and commercial value. Protein refolding is a bottleneck for large‐scale production of valuable proteins expressed as inclusion bodies in Escherichia coli. The denatured rhNTA protein was refolded by an improved size‐exclusion chromatography refolding process achieved by combining an increasing arginine gradient and a decreasing urea gradient (two gradients) with a size‐exclusion chromatography refolding system. The refolding of denatured rhNTA protein showed that this method could significantly increase the activity recovery of protein at high protein concentration. The activity recovery of 37% was obtained from the initial rhNTA protein concentration up to 20 mg/mL. After refolding by two‐gradient size‐exclusion chromatography refolding processes, the refolded rhNTA was purified by ion‐exchange and affinity chromatography. The purified rhNTA protein showed one band in SDS‐PAGE and the specific activity of purified rhNTA protein was 110,000 U/mg. Copyright © 2008 John Wiley & Sons, Ltd.     

Continuous chromatographic protein refolding

Column-based protein refolding requires a continuous processing capability if reasonable quantities of protein are to be produced. A popular column-based method, size-exclusion chromatography (SEC) refolding, employs size-exclusion matrices to separate unfolded protein from denaturant, thus refolding the protein. In this work, we conduct a comparison of SEC refolding with refolding by batch dilution, using lysozyme as a model protein. Lysozyme refolding yield was found to be extremely sensitive to the chemical composition of the refolding buffer and particularly the concentration of dithiothreitol (DTT) introduced from the denatured protein mixture. SEC refolding was not adversely affected by DTT carry-over as small contaminants in the denatured solution are separated from protein during the refolding operation. We also find that, contrary to previous reports, size-exclusion refolding on batch columns leads to refolding yields slightly better than batch dilution refolding yields at low protein concentrations but this advantage disappears at higher protein concentrations. As batch-mode chromatography would be the limiting step in a column based refolding downstream process, the batch column refolding method was translated to a continuously operating chromatography system (preparative continuous annular chromatography, P-CAC). It was shown that the P-CAC elution profile is similar to that of a stationary column, making scale-up and translation to P-CAC relatively simple. Moreover, it was shown that high refolding yields (72%) at high protein concentration (>1 mg ml(-1)) could be obtained.     

On-column refolding of consensus interferon at high concentration with guanidine-hydrochloride and polyethylene glycol gradients

Dilution refolding of consensus interferon (C-IFN) had a limit on final concentration not exceeding 0.1 mg ml(-1) in order to achieve specific activity of 2.2x10(8) U mg(-1). Addition of polyethylene glycol (PEG) only gave a marginal improvement on the specific activity. Hydrophobic interaction chromatography (HIC) was tried but a simple step-wise elution could not refold the protein. Successful refolding was achieved by gradient elution with the decreasing of guanidine-hydrochloride (guanidine-HCl) concentration. The column was packed with a commercially available HIC medium that was designed for protein separation. Polyethylene glycol was found to possess better effect on the column than in the dilution for promotion of correct refolding, especially in gradient mode. A novel dual-gradient strategy, consisting of decreasing guanidine-HCl concentration and increasing PEG concentration, was developed to enhance the refolding yield. Denatured C-IFN was allowed to adsorb and elute from the HIC column through a gradually changed solution environment. Compared with dilution refolding, the gradient HIC process, in the presence of PEG, gave about 2.6-folds of increase in specific activity, 30% increase in soluble protein recovery. Partial purification was also achieved simultaneously.     

Solubilization and Refolding with Simultaneous Purification of Recombinant Human Stem Cell Factor

Recombinant human stem cell factor (rhSCF) was solubilized and renatured from inclusion bodies expressed in Escherichia coli. The effect of both pH and urea on the solubilization of rhSCF inclusion bodies was investigated; the results indicate that the solubilization of rhSCF inclusion bodies was significantly influenced by the pH of the solution employed, and low concentration of urea can drastically improve the solubilization of rhSCF when solubilized by high pH solution. The solubilized rhSCF can be easily refolded with simultaneous purification by ion exchange chromatography (IEC), with a specific activity of 7.8 × 10⁵ IU·mg⁻¹, a purity of 96.3%, and a mass recovery of 43.0%. The presented experimental results show that rhSCF solubilized by high pH solution containing low concentration of urea is easier to be renatured than that solubilized by high concentration of urea, and the IEC refolding method was more efficient than dilution refolding and dialysis refolding for rhSCF. It may have a great potential for large-scale production of rhSCF.     

溶液中变性剂浓度对蛋白溶菌酶复性的影响

Based on three-state renaturation process of denatured proteins, an equation describing the effect of denaturant concentration on renaturation yield of denatured proteins was presented. By this equation, two parameters n（m1 -m2） and Ka can be obtained. The former indicates the difference in the number of denaturant molecules between the renaturation process of n number of refolding intermediates from refolding intermediate state to native state and their aggregate process from refolding intermediate state to aggregate state, the latter denotes the apparent aggregate equilibrium constant for protein molecules aggregated from native state to aggregate state, and from them, the characteristics of the renaturation process of denatured proteins in denaturant solution can be identified. This equation was tested by the renaturation processes of denatured egg white lysozyme in guanidine hydrochloride and urea solutions, with the results to show that when guanidine hydrochloride and urea concentrations were separately higher than 1.25 and 3.00 mol/L or separately lower than 1.00 and 3.00 mol/L, the refolding intermediates of egg white lysozymes were more easily aggregated to aggregate state or more easily renatured to native state, respectively. Under different initial total egg white lysozyme concentrations in urea solution, the refolding egg white lysozyme intermediates could be deduced to have a tendency to form a bimolecular intermediate aggregate, and this inference was further confirmed by their nonreducing SDS-PAGE and size exclusion chromatography.