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.     

Chaperon solvent plug design in size-exclusion chromatography protein refolding process

Although the chaperon solvent plug was reported as a strategy to reduce aggregation before the column inlet in SEC (size-exclusion chromatography) protein refolding process, the appropriate position at which sample injected and the volume of the chaperon solvent plug have not been elucidated. Therefore, the detail of chaperon solvent plug design was investigated in this work. Our results indicated that, to ensure good performances in the SEC refolding process, the appropriate front and tail volumes of chaperon solvent plug should be slightly larger than the optimal values, which depend on the flow dispersion from the injector to the column inlet. However, with the front volume more than the optimum, it could have an adverse effect on activity recovery but not the mass recovery, while no effect at all if the tail volume exceeded the optimum. Furthermore, it might be economical to replace the eluent (refolding buffer) after the tail of chaperon solvent plug with a cheaper one.     

Immunoassay-based determination of phenobarbital using size-exclusion chromatography

The measurement of the anti-epileptic drug phenobarbital from serum samples combining immunoassay and size-exclusion chromatography is presented. The immunoreaction is based on the competitive binding of the analyte (unlabelled phenobarbital) and the fluorescent-labelled phenobarbital to anti-phenobarbital antibodies. Mixing of the reagents and the immunoreaction takes place in a flow system. The products are separated on-line on a short gel chromatographic column and the fluorescence intensity of the marker is measured. The calibration curve shows good linearity in the range 5–80 μg/ml, corresponding to therapeutically relevant serum levels. Intra-day precision values are between 7.32 and 9.48%; the accuracy is between 0.97 and 9.43%. Inter-day precision and accuracy measured on 6 different days fall between 5.38 and 10.05% and −8.27 and −4.97%, respectively. The results obtained with the proposed method show a good correlation with those of other methods (radioimmunoassay and fluorescence polarisation immunoassay) already established in clinical laboratories.     

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.     

Surfactant-induced refolding of lysozyme

The surfactant-lysozyme interaction was investigated by circular dichroism, fluorescence, UV, dynamic light scattering, surface tension, turbidity measurements and lysozyme activity assay. A new way of refolding of lysozyme was found. It was shown that the lysozyme unfolded by anionic surfactants could be renatured by adding cationic surfactants. That is, lysozyme formed precipitate with anionic surfactants, the precipitates could be dissolved by adding a cationic surfactant solution, and then the lysozyme was refolded to its native state spontaneously. Different couples of anionic surfactants and cationic surfactants including C10SO3/C10NE, C12SO3/C10NE, C10SO3/C12NE, C10SO3/C12NB, C10SO4/C10NE and C12SO4/C10NE (C(n)SO3, C(n)SO4, C(n)NE and C(n)NB represent sodium alkyl sulfonate/sulfate, alkyl triethyl/butyl ammonium bromide respectively) were investigated, all of them gave similar results. The results were explained in terms of the differences between the interaction of anionic-cationic surfactants and that of surfactant-lysozyme. It was thought that the formation of mixed micelles of anionic-cationic surfactants is a more favorable process than that of lysozyme-surfactant complexes, which induces the dissociation of lysozyme-surfactant complexes when cationic surfactants were added.     

Molecularly imprinted polymer-assisted refolding of lysozyme

For production of active proteins using heterologous expression systems, refolding of proteins from inclusion bodies often creates a bottleneck due to its poor yield. In this study, we show that molecularly imprinted polymer (MIP) toward native lysozyme promotes the folding of chemically denatured lysozyme. The MIP, which was prepared with 1 M acrylamide, 1 M methacrylic acid, 1 M 2-(dimethylamino)ethyl methacrylate, and 5 mg/mL lysozyme, successfully promoted the refolding of lysozyme, whereas the non-imprinted polymer did not. The refolding yield of 90% was achieved when 15 mg of the MIP was added to 0.3 mg of the unfolded lysozyme. The parallel relationship between the refolding yield and the binding capacity of the MIP suggests that MIP promotes refolding through shifting the folding equilibrium toward the native form by binding the refolded protein.     

Critical analysis of lysozyme refolding kinetics

The kinetics of lysozyme refolding and aggregation is studied using an existing competing first- and third-order reaction scheme. The existing model overestimates yield at high refolding concentrations (>1 mg/mL), thus limiting its use for reactor design at industrially relevant refolding concentrations. This study demonstrates that a pathway exists for the incorporation of refolded native protein into aggregates. Specifically, native lysozyme labeled with fluorescein isothiocyanate was added to the refolding buffer prior to dilution refolding of denatured and reduced lysozyme. Aggregates collected from these experiments showed significant fluorescence, indicating that labeled lysozyme had been incorporated into the aggregates during refolding. Although the precise pathway of incorporation has not been elucidated, it is clear from this work that the existing model for lysozyme refolding is not globally applicable. In particular, previous work has analytically demonstrated that neglect of a pathway from native to aggregate can result in the design of a grossly suboptimal reactor strategy. This study demonstrates that such a pathway can exist experimentally and emphasizes the need to critically assess refolding kinetic models before their use in reactor design equations.     

Effect of column dimensions and flow rates on size-exclusion refolding of beta-lactamase

We have investigated the effect of changing the column diameter and length on the size exclusion chromatography (SEC) refolding of beta-lactamase from Escherichia coli-derived inclusion bodies (IBs). Inclusion bodies were recovered and solubilised in 6 M GdnHCl and 5 mM DTT. Up to 16 mg of denatured, solubilised beta-lactamase was loaded onto size exclusion columns packed with Sephacryl S-300 media (fractionation range: 10(4)-1.5 x 10(6) Da). beta-Lactamase was refolded by eluting the loaded sample with 1 M urea in 0.05 M phosphate buffer, pH 7 at 23 degrees C. The following columns were studied: 26 x 400, 16 x 400 and 26 x 200 mm, with a range of mobile phase flow rates from 0.33 to 4.00 ml/min. beta-Lactamase was successfully refolded in all three columns and at all flow rates studied. The beta-lactamase activity peak coincided with the major protein peak. Reducing the column diameter had little effect on refolding performance. The enzyme activity recovered was relatively independent of the mobile phase linear velocity. Reducing the column length gave a poorer resolution of the protein peaks, but the enzyme activity peaks were well resolved. Calculation of the partition coefficients for beta-lactamase activity showed that the 26 x 400 column gave the greatest refolding performance.     

Temperature-responsive size-exclusion chromatography using poly(N-isopropylacrylamide) grafted silica

Silica-based packing materials induce non-specific interactions with proteins in aqueous media because of the nature of their surface, mainly silanol groups. Therefore, the silica surface has to be modified in order to be used as stationary phase for the High Performance Size-Exclusion Chromatography (HPSEC) of proteins. For this purpose, porous silica beads were coated with hydrophilic polymer gels (dextrans of different molecular weights) carrying a calculated amount of diethylaminoethyl groups (DEAE). Actually, as shown by HPSEC, these dextran modified supports minimize non-specific adsorption for proteins and pullulans in aqueous solution. Then, in order to change the pore size in response to temperature, temperature responsive polymer of poly(N-isopropylacrylamide) (PIPAAm) was introduced into the surface of dextran-DEAE on porous silica beads. The structure of these supports before and after modification was alternately studied by Scanning Electronic Microscopy (SEM) and Scanning Force Microscopy (SFM). An adsorption of radiolabelled albumin was performed to complete our study. Silica modifications by dextran-DEAE and PIPAAm improve the neutrality of the support and minimize the non-specific interactions between the solid support and proteins in solution. At low temperature, the support having PIPAAm exhibits a high resolution domain in HPSEC and finally permits a better resolution of proteins and pullulans. At higher temperature, hydrophobic properties of PIPAAm produce interactions with some proteins and trigger off a slight delay of their elution time.     

On-column refolding of denatured lysozyme by the conjoint chromatography composed of SEC and immobilized recombinant DsbA

DsbA (disulfide bond formation protein A) located in the periplasm of Escherichia coli is a disulfide isomerase, which is vital to disulfide bonds formation directly affecting the nascent peptides folding to the correct conformation. In this paper, recombinant DsbA was firstly immobilized onto NHS-activated Sepharose Fast Flow gel. Then Sephadex G-100 gel was sequentially packed on the top of recDsbA Sepharose Fast Flow, and a so-called conjoint chromatography column composed of SEC and immobilized recombinant DsbA was constructed. Denatured lysozyme was applied on the conjoint column. The effect of SEC volume, flow rate, loading amount and volume, pre-equilibrium mode and KCl concentration in the buffer on lysozyme refolding were investigated in detail and the stability of DsbA immobilization was evaluated. Finally the reusability of the conjoint refolding column was also tested. When loading 2.4 mg denatured lysozyme in 0.5 ml solution, the activity recovery reached 92.7% at optimized experimental conditions, and the conjoint column renaturation capacity decreased only 7.7% after six run reuse due to the use of SEC section in the chromatographic refolding process. The conjoint chromatography offers an efficient strategy to refold proteins in vitro with high productivity and column reusability.     

Oxidative refolding of amyloidogenic variants of human lysozyme

The oxidative refolding of human lysozyme and its two best characterised amyloidogenic variants, Ile56Thr and Asp67His, has been investigated in vitro by means of the concerted application of a range of biophysical techniques. The results show that in each case the ensemble of reduced denatured conformers initially collapses into a large number of unstructured intermediates with one or two disulphide bonds, the majority of which then fold to form the native-like three-disulphide intermediate, des-[77-95]. The slow step in the overall folding reaction involves the rearrangement of the latter to the fully oxidised native protein containing four disulphide bonds. The Ile56Thr and Asp67His variants were found to fold faster than the wild-type protein by a factor of 2 and 3 respectively, an observation that can be attributed primarily to the reduction in the barriers to conformational rearrangements that results from both the mutations. The efficient folding of these variants despite their enhanced propensities to aggregate when compared to the wild-type protein is consistent with their ability to be secreted in sufficient quantities to give rise to the systemic amyloidoses with which they are associated.     

Preparative size-exclusion chromatography of human serum apolipoproteins using an analytical liquid chromatograph

Apolipoproteins, extracted from human serum high-density lipoproteins, can be resolved and recovered with high yield from a preparative MicroPak TSK Type 3000SW size-exclusion column using Tris-buffered 6 m urea or 6 m guanidinium chloride mobile phases. Adequate resolution of some apolipoprotein pairs is only achieved at low flow velocities and low sample loads, necessitating repetitive injections of small amounts of material for preparative isolation. An analytical high-performance liquid chromatograph equipped with a simplified sample introduction scheme and low-pressure switching valves for fraction collection was used to isolate milligram quantities of HDL apolipoproteins.     

A near-native state on the slow refolding pathway of hen lysozyme

The refolding of four disulfide lysozyme (at pH 5.2, 20 degrees C) involves parallel pathways, which have been proposed to merge at a near-native state. This species contains stable structure in the alpha- and beta-domains but lacks a functional active site. Although previous experiments have demonstrated that the near-native state is populated on the fast refolding pathway, its relevance to slow refolding molecules could not be directly determined from previous experiments. In this paper, we describe experiments that investigate the effect of added salts on the refolding pathway of lysozyme at pH 5.2, 20 degrees C. We show, using stopped flow tryptophan fluorescence, inhibitor binding, and circular dichroism (CD), that the rate of formation of native lysozyme on the slow refolding track is significantly reduced in solutions of high ionic strength in a manner dependent on the position of the anion in the Hofmeister series. By contrast, the rate of evolution of hydrogen exchange (HX) protection monitored by electrospray ionization mass spectrometry (ESI MS) is unchanged under the refolding conditions studied. The data show, therefore, that at high ionic strengths beta-domain stabilization and native state formation on the slow refolding pathway become kinetically decoupled such that the near-native state becomes significantly populated. Thus, by changing the energy landscape with the addition of salts new insights into the relevance of intermediate states in lysozyme refolding are revealed.     

Determination of polyanionic macromolecules by size-exclusion chromatography

This report presents an extension of a method developed for determination of dextran sulfate in rat serum. The drug is a negatively charged polysaccharide with a molecular mass of 8000. It is fractionated by molecular size and separated from serum components by high-performance size-exclusion chromatography. Sensitive detection is achieved by the post-column complexation of the analyte with 1,9-dimethylmethylene blue (DMMB). A metachromatic complex is formed; the absorbance maximum of the complex is shifted from that of the free dye. Various glycosaminoglycans and other macromolecular polyanions interact with DMMB. Several can be determined using the chromatographic conditions developed for dextran sulfate. The method provides a simple procedure for quantitation of these compounds. Compared to spectrophotometric assays, less sample preparation is required, selectivity is enhanced, and molecular mass information is provided. With modification of eluent composition, dye concentration, and detection wavelength, the method can be validated for determination of additional compounds.     

Calcium-dependent changes in properties of human prothrombin: A study using high-performance size-exclusion chromatography and gel-permeation chromatography

High-performance size-exclusion chromatography using a TSK 3000 SW column and aqueous gel filtration with Sephacryl S-200 SF have been used to characterize the effects of calcium ions on the hydrodynamic properties of human prothrombin and prethrombin 1. The results suggest that the effective hydrodynamic radius of prothrombin is less in the presence than in the absence of calcium ions. In addition, when using the TSK-3000 SW column, Ca²⁺-dependent formation of a hydrophobic site in the fragment 1 region of prothrombin results in an apparent further decrease in hydrodynamic radius.     

Anaerobic acidogenesis of a complex wastewater: I. The influence of operational parameters on reactor performance

The influence of operational, parameters, such as hydraulic retention time, organic loading rate, influent substrate concentration, pH, and temperature, on the performance of the first phase of anaerobic digestion has been investigated. A complex substrate based on beef extract was used, and six series of experimental runs were conducted, each one showing the effect of one operational variable. The predominant fermentation products were always acetic and propionic acid, independent of the values of the operational parameters. For initial COD concentrations and hydraulic retention times above the critical values identified as 3 g/L and 6 h, respectively, the degree of acidification achieved was between 30 and 60%. The degree of acidification was found to increase with the hydraulic retention time and decrease with the influent substrate concentration and organic loading rate, while the opposite held true for the rate of product formation. Furthermore, it has been demonstrated that acidification is primarily determined by the hydraulic retention time and the rate of product formation by the influent substrate concentration. The concentration of the acetic acid produced was found to depend on the operational parameters. However, the concentration of propionic acid produced depended only on the substrate availability with a consistent proportion of 8% initial COD converted to it. The optimum pH and temperature were 7 and 40 degrees C, respectively. The percentage of acetic acid as a proportion of the total volatile fatty acids produced was found to increase with increasing pH and temperature, while the percentage of propionic acid seemed to decrease accordingly. Finally the effect of the temperature on the rate of acidification followed an Arrhenius type equation with an activation energy equal to 4739 cal/mol.     

Refolding of denatured thioredoxin observed by size-exclusion chromatography

Molecular sieve chromatography can resolve interactive systems into populations having different effective hydrodynamic volumes. In this report, the advantages of such resolution to protein folding are illustrated by using moderate pressure to decrease analysis time and lowered temperature to slow down the kinetics of conformational change. A 300-mm Bio-Sil TSK-125 size-exclusion column was equilibrated with a series of different concentrations of guanidine hydrochloride at 2 degrees C in 50 mM phosphate buffer, pH 7.0. Samples of native Escherichia coli thioredoxin, denatured thioredoxin, or thioredoxin equilibrated with the column solvent were injected, and the effluent was monitored at 220 nm. Injection of equilibrated protein samples defined three denaturant concentration zones identical with those observed by spectral measurements: the native base-line zone where only compact protein is observed in the effluent profile; the transition zone in which both compact and denatured forms are observed in slow exchange; and the denatured base-line zone in which only denatured protein is observed. Unfolding was observed by injection of native protein into columns having isocratic denaturant concentrations in the transition and denatured base-line zones. Effluent profiles indicated a dynamic conversion of compact to denatured protein with a time constant which appeared to decrease markedly with increasing denaturant concentration. Refolding was observed by injection of denatured protein into columns having isocratic concentrations in the transition and native base-line zones. As the denaturant concentration was decreased, the effluent profiles evidenced a persistent slow conversion of denatured to compact protein which was suddenly accelerated about midway in the native base-line zone.(ABSTRACT TRUNCATED AT 250 WORDS)     

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.