Renaturation of Escherichia coli-derived recombinant human macrophage colony-stimulating factor.

Recombinant human macrophage colony-stimulating factor (rhM-CSF), a homodimeric, disulfide bonded protein, was expressed in Escherichia coli in the form of inclusion bodies. Reduced and denatured rhM-CSF monomers were refolded in the presence of a thiol mixture (reduced and oxidized glutathione) and a low concentration of denaturing agent (urea or guanidinium chloride). Refolding was monitored by nonreducing gel electrophoresis and recovery of bioactivity. The effects of denaturant type and concentration, protein concentration, concentration of thiol/disulfide reagents, temperature, and presence of impurities on the kinetics of rhM-CSF renaturation were investigated. Low denaturant concentrations (<0.5 M urea) and high protein concentrations (>0.4 mg/ml) in the refolding mixture resulted in increased formation of aggregates, although aggregation was never significant even when refolding was carried out at room temperature. Higher protein concentration resulted in higher rates but did not lead to increased yields, due to the formation of unwanted aggregates. Experiments conducted at room temperature resulted in slightly higher rates than those conducted at 4 degrees C. Although the initial renaturation rate for solubilized inclusion body protein without purification was higher than that of the reversed-phase purified reduced denatured rhM-CSF, the final renaturation yield was much higher for the purified material. A maximum refolding yield of 95% was obtained for the purified material at the following refolding conditions: 0.5 M urea, 50 mM Tris, 1.25 mM DTT, 2 mM GSH, 2 mM GSSG, 22 degrees C, pH 8, [protein] = 0.13 mg/ml.     

Refolding of denatured/reduced lysozyme at high concentration with diafiltration

Refolding of reduced and denatured protein in vitro has been an important issue for both basic research and applied biotechnology. Refolding at low protein concentration requires large volumes of refolding buffer. Among various refolding methods, diafiltration is very useful to control the denaturant and red/ox reagents in a refolding solution. We constructed a refolding procedure of high lysozyme concentration (0.5-10 mg/ml) based on the linear reduction of the urea concentration during diafiltration under oxygen pressure. When the urea concentration in the refolding vessel was decreased from 4 M with a rate of 0.167 M/h, the refolding yields were 85% and 63% at protein concentrations, 5 mg/ml and 10 mg/ml, respectively, after 11 h. This method gave a high productivity of 40.1,microM/h of the refolding lysozyme. The change in refolding yields during the diafiltration could be simulated using the model of Hevehan and Clark.     

Mechanism of pH‐sensitive polymer‐assisted protein refolding and its application in TGF‐β1 and KGF‐2

Refolding of proteins at high concentrations often results in non‐productive aggregation. This study, through a unique combination of spectroscopic and chromatographic analyzes, provides biomolecular evidence to demonstrate the ability of Eudragit S‐100, a pH‐responsive polymer, to enhance refolding of denatured‐reduced lysozyme at high concentrations. The addition of Eudragit in the refolding buffer significantly increases lysozyme refolding yield to 75%, when dilution refolding was conducted at 1 mg/mL lysozyme. This study shows evidence of an electrostatic interaction between oppositely charged lysozyme and the Eudragit polymer during refolding. This ionic complexing of Eudragit and lysozyme appears to shield exposed hydrophobic residues of the lysozyme refolding intermediates, thus minimizing hydrophobic‐driven aggregation of the molecules. Importantly, results from this study show that the Eudragit‐lysozyme bioconjugation does not compromise refolded protein structure, and that the polymer can be readily dissociated from the protein by ion exchange chromatography. The strategy was also applied to refolding of TGF‐β1 and KGF‐2. © 2009 American Institute of Chemical Engineers Biotechnol. Prog. 2009     

Refolding and characterization of rat liver methionine adenosyltransferase from Escherichia coli inclusion bodies

Methionine adenosyltransferase (MAT) catalyzes the synthesis of S-adenosylmethionine, the major methyl donor for transmethylation reactions. Attempts to perform structural studies using rat liver MAT have met with problems because the protein purified from cellular extracts is heterogeneous. Overexpression of the enzyme in Escherichia coli rendered most of the protein as inclusion bodies. These aggregates were purified by specific washes using urea and Triton X-100 and used for refolding. Maximal activity was obtained when chaotropic solubilization included the structural cation Mg(2+), the protein concentration was kept below 0.1 mg/ml, and denaturant removal was carried out in a two-step process, namely, a fast dilution followed by dialysis in the presence of 10 mM DTT or GSH/GSSG redox buffers. Refolding by this procedure generated the oligomeric forms, MAT I and III, which were basically indistinguishable from the purified rat liver forms in secondary structure and catalytic properties.     

Effect of surface concentration on secondary and tertiary conformational changes of lysozyme adsorbed on silica nanoparticles

Kinetics of tertiary conformation of lysozyme adsorbed on 90 nm silica nanoparticles was inferred using tryptophan fluorescence for different surface concentrations (0.24 to 0.92 mg/m(2)), pH (4, 7 and 9), ionic strength (10 and 100 mM), 2,2,2-trifluoroethanol (TFE) (5, 15 and 30%) and Dithiothreitol (DTT) (0.5 mg/ml) concentrations. A rapid initial unfolding, followed by a much slower refolding and subsequent unfolding, were observed with the extent of unfolding being higher at lower surface concentration, higher ionic strengths, higher TFE and DTT concentrations and at pH 9. The rate of unfolding was found to be higher at lower surface concentrations, pH 4, higher ionic strengths, higher TFE and DTT concentrations. In contrast, earlier results showed that beta lactoglobulin unfolded slower and exhibited only an initial rapid and a subsequent slow unfolding phase. Circular Dichroism spectra showed that alpha helix content was lower for adsorbed lysozyme compared to bulk with a corresponding increase in beta sheet and random coil. This decrease in alpha helix was found to be more pronounced at lower surface concentrations. DTT decreased alpha helix with a corresponding increase in random coil while TFE was found to have negligible effect on secondary structure.     

Inclusion body purification and protein refolding using microfiltration and size exclusion chromatography

The presence of inclusion body impurities can affect the refolding yield of recombinant proteins, thus there is a need to purify inclusion bodies prior to refolding. We have compared centrifugation and membrane filtration for the washing and recovery of inclusion bodies of recombinant hen egg white lysozyme (rHEWL). It was found that the most significant purification occurred during the removal of cell debris. Moderate improvements in purity were subsequently obtained by washing using EDTA, moderate urea solutions and Triton X-100. Centrifugation between each wash step gave a purer product with a higher rHEWL yield. With microfiltration, use of a 0.45 micron membrane gave higher solvent fluxes, purer inclusion bodies and greater protein yield as compared with a 0.1 micron membrane. Significant flux decline was observed for both membranes. Second, we studied the refolding of rHEWL. Refolding from an initial concentration of 1.5 mg ml-1, by 100-fold batch dilution gave a 43% recovery of specific activity. Purified inclusion bodies gave rise to higher refolding yields, and negligible activity was observed after refolding partially purified material. Refolding rHEWL with a size exclusion chromatography based process gave rise to a refolding yield of 35% that corresponded to a 20-fold dilution.     

Refolding human serum albumin at relatively high protein concentration

The conditions for refolding reduced and denatured human serum albumin (HSA) were investigated with a view to maximising the yield of native monomeric albumin. Refolding by dialysis was found to be preferable to dilution as a means of chaotrope (urea) and reductant (2-mercaptoethanol) removal. Dialysis of denatured HSA solutions containing 4-8 M urea and 14 mM 2-mercaptoethanol at pH 10.0 was found to be optimal for HSA refolding. The yield of monomeric HSA was maximal (94%) for dialysis in the presence of EDTA (1 mM) and sodium palmitate (20 microM). Using this protocol it was possible to refold HSA at concentrations in excess of 5 mg.ml-1 whilst maintaining a high recovery of native monomer. These results represent a considerable improvement on established methods of HSA refolding.     

Efficient lysozyme refolding at a high final concentration and a low dilution factor

Of the various protein refolding methods, direct dilution is one of the simplest and easiest for scaling up the refolding process. However, it requires a large amount of refolding buffer, often utilizes a number of chemicals, and results in a low final protein concentration. In this report, we demonstrate that reduced dithiothreitol (DTT^red), a carryover from denaturation, is a crucial and adverse factor in lysozyme refolding. Accordingly, we proposed a method of using high concentration of oxidized glutathione (GSSG) in the refolding buffer to eliminate excess DTT^red and aid in the refolding of lysozyme. The efficiency of this method is 84%, which resulted in a high final refolded protein concentration of 1.5 g/l and required only a low dilution factor (4×). Furthermore, compared with the traditional 50× direct dilution (resulting in a similar yield of 74%), the low dilution factor required much less GSSG and other constituents.     

Protein refolding at high concentration using size-exclusion chromatography

A new method to improve refolding yields and to increase the concentration of refolded proteins in a single operation has been developed. The method uses size-exclusion chromatography matrices to perform buffer exchange, aggregate removal, and the folding reaction. The reduced diffusion of proteins in gel-filtration media has been shown to suppress the nonspecific interactions of partially folded molecules, thus reducing aggregation. Hen egg white lysozyme (HEWL) and bovine carbonic anhydrase (CAB) were successfully refolded from initial protein concentrations of up to 80 mg/mL using Sephacryl S-100 (HR). The aggregation reaction for lysozyme was reduced and was only detected at the highest protein concentration used. The average recovery of lysozyme was 63%, with an average specific activity of 104%. Carbonic anhydrase experiments also showed that aggregation was suppressed and the average protein recovery from the column was 56%, with a specific activity of 81%. This process enables refolding and the purification of active species to be achieved in a single step. (c) 1996 John Wiley & Sons, Inc.     

Production of Leptin inEscherichia coli:A Comparison of Methods

A procedure is described for gram-scale refolding ofEscherichia coli-derived human leptin inclusion bodies. Refolding was achieved by gradually reducing denaturant using a diafiltration method. Refolded leptin is characterized byin vivomodulation of food intake, reduction in body weight, and lowering of insulin and glucose levels inob/obmice. In addition, refolded leptin is characterized by radioimmunoassay (RIA) and activation of the leptin receptor in a cell-based assay. For comparison we also refolded leptin by a simple dilution method and produced periplasmic derived leptin, which did not requireex vivofolding. Leptin produced by these three methods and leptin obtained from commercial sources were compared using the RIA and the cell-based assay and appeared to be of comparable quality and potency.     

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.     

Refolding and aggregation of bovine carbonic anhydrase B: quasi-elastic light scattering analysis

Bovine carbonic anhydrase B (CAB) is chosen as the model protein to study the phenomenon of protein aggregation, which often occurs during the refolding process. Refolding of CAB from 5 M GuHCl has been observed by quasi-elastic light scattering (QLS), which confirms the formation of a molten globular protein structure as reported previously [Semisotnov, G. V., Rodionova, N. A., Kutyshenko, V. P., Ebert, B., Blanck, J., & Ptitsyn, O. B. (1987) FEBS Lett. 224, 9-13]. QLS analysis reveals the formation of multimeric species prior to precipitation. Activity and cross-linking studies have confirmed the presence of inactive multimeric protein species. The dimer formation has been determined to be the initiating step in the aggregation of CAB during refolding. Activity studies have indicated that the first intermediate observed in the refolding pathway of CAB aggregates to form the inactive dimer. The rate of formation of the dimer has a stoichiometric dependence on the final protein concentration. The dimer formation rate is a function of the final guanidine hydrochloride (GuHCl) concentration to the inverse 6.7 power, which correlates well with the binding of GuHCl to the native protein in 0.60-0.80 M GuHCl. These rate dependencies require the refolding of CAB to be performed at high GuHCl concentrations (1 M GuHCl) and low protein concentrations (less than 1 mg/mL) to avoid the formation of aggregates. Alternatively, refolding can be performed by allowing the first intermediate to form the second intermediate prior to further dilution or dialysis. The aggregation of a hydrophobic first intermediate species is likely to be common to the refolding of other molten globular proteins.     

Acyl cystamine: small-molecular foldase mimics accelerating oxidative refolding of disulfide-containing proteins

Based on the structural characteristic of Protein disulfide isomerases and DsbA that have hydrophobic regions around the active sites, hydrophobic alkyl tails are linked to cystamine to create new small molecular foldase mimics, acyl cystamine. Both the oxidizing power and oxidation specificity of cystamine are enhanced by n-octanoyl or n-hexanoyl tail. N-octanoyl and n-hexanoyl cystamine are very effective to facilitate oxidative protein refolding at strong reducing environments. In the presence of 0.42 mM DTT, the activity recovery of lysozyme is over 90% by 90-min refolding with 0.1 mM n-octanoyl cystamine and 0.1 mM cystamine as oxidant, while almost no activity is recovered with 0.2 mM GSSG by 160-min refolding. For the refolding of 0.2 mg/mL lysozyme, with 0.6 mM n-hexanoyl cystamine and 1.12 mM residual DTT as redox agents, the activity recovery reaches as high as 93% after refolding for only 20 min. For ribonuclease A (RNase A) refolding, with 0.4 mM n-hexanoyl cystamine and 1.30 mM DTT, the recovery of activity reaches as high as 90% within 3 h. Thus, with n-octanoyl or n-hexanoyl cystamine as the oxidants, the necessity to remove excess DTT in the reduced and denatured protein solutions can be greatly alleviated. With a moderate hydrophobicity, n-hexanoyl cystamine is promising for application in oxidative protein refolding at an extensive concentration range. It is observed that in the oxidative refolding of 0.2 mg/mL lysozyme and RNase A, only about half of n-hexanoyl cystamine is needed when compared to cystamine to achieve the same kinetic effect.     

The influence of operational parameters on lysozyme refolding using size-exclusion chromatography

The influence of several parameters on the gel filtration refolding of hen egg white lysozyme from a starting concentration of 40 mg/ml was investigated. Refolding was found to be unaffected by temperature between 30 and 50°C, giving 100% recovered specific activity. At 10°C a 20% reduction in refolding yield was observed. Refolding was carried out successfully with both acrylamide (Sephacryl S100)- and dextran (Superdex 75)-based gel media. At the isoelectric pH of lysozyme, aggregation was suppressed in the column method, whereas protein aggregates were formed during dilution-based refolding. A number of compounds (carboxymethyl cellulose, dextran, sucrose) were added to the mobile phase to reduce the relative viscosity between the sample and mobile phase. Only sucrose, up to 20% (wt), was found not to interfere with lysozyme refolding.     

Unfolding the unique c-type heme protein, Chlamydomonas reinhardtii cytochrome f

We have studied the unfolding reaction of cytochrome f from the green alga Chlamydomonas reinhardtii. Cytochrome f is different from all other c-type heme proteins in that it is a large, two-domain protein with predominantly beta-sheet structure. Moreover, the sixth axial ligand to the heme-iron is unique in cytochrome f: it is provided by the N-terminal alpha-amino group. Unfolding of oxidized and reduced cytochrome f by guanidine hydrochloride (GuHCl) was monitored by far-UV circular dichroism (CD), Soret absorption, and tyrosine emission: the same unfolding curves were obtained regardless of method. Neither oxidized nor reduced unfolded cytochrome f can be refolded at neutral pH. At pH 3.5 refolding takes place (upon dilution to lower denaturant concentrations or by electron injection to the unfolded, oxidized form), although the reaction is extremely slow. Reduced cytochrome f appears much more resistant towards denaturant perturbation than the oxidized form (in pH range 7-3.5). The heme in unfolded cytochrome f remains low-spin to pH 4 but turns high-spin at pH 3.5 (presumably due to protonation of the N-terminal amino group). Our results suggest that the unfolding process for cytochrome f is complex, involving kinetically trapped intermediates not resolvable by spectroscopy.     

Computer Simulation and Additive-Based Refolding Process of Cysteine-Rich Proteins: VEGF-A as a Model

Refolding of cysteine-rich protein for establishing native conformation and a biologically active form is the most challenging step in recombinant protein synthesis. In this study, expressed vascular endothelial growth factor-A (VEGF-A), as a cysteine-rich protein, in a prokaryotic expression cell was refolded based on computer simulation technique and multiple chemical additive-based buffers to recover its biologically active form. For this purpose, cloned and expressed VEGF-A in Escherichia coli BL21 (DE3) was purified and dialyzed by a basic buffer containing nine diverse chemical additives. In parallel with the evaluations of the applied additives, professional computer simulation software was also used. The activity of refolded protein was evaluated in differentiation of mesenchymal stem cells (MSCs) to the endothelial cells (ECs). The results showed that dialyzing the produced recombinant VEGF-A in chemical additive-based buffers containing cysteine, 1, 4-dithiothreitol (DTT), arginine, and Triton X-100 led to efficient VEGF-A refolding. The results of flowcytometry analysis indicated that CD31 and CD144 as the specific ECs markers in VEGF-A treated MSCs were 31 and 73%, respectively. Protein refolding method using chemical additive-based buffers containing cysteine, DTT, arginine and Triton X-100 was the best accessible technique for refolding cysteine-rich recombinant VEGF-A.     

High-pressure refolding of disulfide-cross-linked lysozyme aggregates: thermodynamics and optimization

Previous exploratory work revealed that high pressure (200 MPa), in combination with oxido-shuffling agents such as glutathione, effectively refolds covalently cross-linked aggregates of lysozyme into catalytically active native molecules, at concentrations up to 2 mg/mL (1). To understand further and optimize this process, in the current study we varied the redox conditions and levels of guanidine hydrochloride (GdnHCl) in the refolding buffer. Maximum refolding yields of 80% were seen at 1 M GdnHCl; higher concentrations did not increase refolding yields further. A maximum in refolding yield was observed at redox conditions with a 1:1 ratio of oxidized to reduced glutathione (GSSG:GSH). Yields decreased dramatically at more oxidizing conditions ([GSSG] > [GSH]). Kinetics of dissolution and refolding of covalently cross-linked aggregates of lysozyme depended strongly on redox conditions. At GSSG:GSH ratios of 4:1, 1:1, and 1:16, lysozyme dissolved and refolded with time constants of 62, 20, and 8 h, respectively. Estimates of the free energy of unfolding of lysozyme in GdnHCl solutions at 200 MPa suggested that the native state of lysozyme is strongly favored (ca.18.6 kJ/mol) under the conditions used for dissolution and refolding.     

Protein refolding mediated by reverse micelles of Cibacron Blue F-3GA modified nonionic surfactant

An affinity-based reverse micellar system formulated with nonionic surfactant was applied to the refolding of denatured-reduced lysozyme. The nonionic surfactant of sorbitan trioleate (Span 85) was modified with Cibacron Blue F-3GA (CB) as an affinity surfactant (CB-Span 85) to form affinity-based reverse micelles in n-hexane. The water content of 15 was found optimal for lysozyme refolding in the reverse micellar system of 62.7 mmol/L Span 85 with coupled CB of 0.3 and 0.5 mmol/L. In addition, the operating conditions such as pH and the concentrations of urea and redox reagents were optimized. Under the optimized conditions, complete renaturation of lysozyme at 3-3.5 mg/mL was achieved, whereas dilution refolding in the bulk aqueous phase under the same conditions gave much lower activity recovery. Moreover, the secondary structure of the refolded lysozyme was found to be the same as the native lysozyme. Over 95% of the refolded lysozyme was recovered from CB-Span 85 reverse micelles by a stripping solution of 0.5 mol/L MgCl(2). Thus, the present system is advantageous over the conventional reverse micellar system formed with ionic surfactants in the ease of protein recovery.     

Reshaping the folding energy landscape by chloride salt: impact on molten-globule formation and aggregation behavior of carbonic anhydrase

During chemical denaturation different intermediate states are populated or suppressed due to the nature of the denaturant used. Chemical denaturation by guanidine-HCl (GuHCl) of human carbonic anhydrase II (HCA II) leads to a three-state unfolding process (Cm,NI=1.0 and Cm,IU=1.9 M GuHCl) with formation of an equilibrium molten-globule intermediate that is stable at moderate concentrations of the denaturant (1-2 M) with a maximum at 1.5 M GuHCl. On the contrary, urea denaturation gives rise to an apparent two-state unfolding transition (Cm=4.4 M urea). However, 8-anilino-1-naphthalene sulfonate (ANS) binding and decreased refolding capacity revealed the presence of the molten globule in the middle of the unfolding transition zone, although to a lesser extent than in GuHCl. Cross-linking studies showed the formation of moderate oligomer sized (300 kDa) and large soluble aggregates (>1000 kDa). Inclusion of 1.5 M NaCl to the urea denaturant to mimic the ionic character of GuHCl leads to a three-state unfolding behavior (Cm,NI=3.0 and Cm,IU=6.4 M urea) with a significantly stabilized molten-globule intermediate by the chloride salt. Comparisons between NaCl and LiCl of the impact on the stability of the various states of HCA II in urea showed that the effects followed what could be expected from the Hofmeister series, where Li+ is a chaotropic ion leading to decreased stability of the native state. Salt addition to the completely urea unfolded HCA II also led to an aggregation prone unfolded state, that has not been observed before for carbonic anhydrase. Refolding from this state only provided low recoveries of native enzyme.     

Refolding of partially and fully denatured lysozymes

Lysozyme refolding with high yields sometimes results from incomplete denaturation. Dithiothreitol (DTT) is a reductant commonly used to reduce and unfold disulfide-stabilized lysozymes. Through the use of fluorescence spectroscopy to access the extent of denaturation, we found that the rate and extent of denaturation highly depended on the concentration of DTT. Further, the denaturation exhibited a two-phase transition at a high DTT concentration with DTT at >100 mM and long denaturation time (>24 h) being needed for complete denaturation. A low DTT concentration and a short denaturation time resulted in fast refolding with high activity recovery, while a high DTT concentration and a long denaturation time resulted in slow refolding with low activity recovery. Hence, the renaturation of disulfide-containing lysozyme was highly affected by the extent of denaturation.