Journal of Surface Engineered Materials and Advanced Technology
Vol.4 No.1(2014), Article ID:42048,5 pages DOI:10.4236/jsemat.2014.41002

Efficient Protein Refolding Using Surfactants at High Final Protein Concentration

Hidetaka Noritomi*, Yoshiyuki Kato, Satoru Kato

Department of Applied Chemistry, Tokyo Metropolitan University, Tokyo, Japan.

Email: *noritomi@tmu.ac.jp

Copyright © 2014 Hidetaka Noritomi et al. This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited. In accordance of the Creative Commons Attribution License all Copyrights © 2014 are reserved for SCIRP and the owner of the intellectual property Hidetaka Noritomi et al. All Copyright © 2014 are guarded by law and by SCIRP as a guardian.

Received December 11th, 2013; revised January 2nd, 2014; accepted January 13th, 2014

ABSTRACT

The refolding of denatured hen egg white lysozyme (HEWL) was examined by surfactants at a high final refolded HEWL concentration (1 mg/mL). Hexadecyltrimethylammonium bromide (CTAB) and sucrose fatty acid monoester (DK-SS) were used to dissolve denatured HEWL without denaturants such as guanidine hydrochloride (GuHCl) and urea. When denatured HEWL was perfectly dissolved in buffer solutions containing surfactants and dithiothreitol (DTT), the concentration of CTAB was about one-twentieth times less than that of DK-SS. The concentration of CTAB strongly affected the refolding yield, and the maximum refolding yield was obtained at 0.88 mM CTAB, which is around the critical micelle concentration of CTAB. The refolding yield was influenced by the molar ratio of oxidized glutathione (GSSG) to DTT, and the maximum refolding yield was obtained when [GSSG]/[DTT] was 1.5. The refolding yield was markedly dependent upon the solution pH of HEWL, and exhibited 80% at pH 5.2.

Keywords: Protein Refolding; Dilution Method; Surfactant; Hen Egg-White Lysozyme

1. Introduction

Surfactants are amphiphilic substances that consist of hydrophobic groups and hydrophilic groups [1]. Due to the amphiphilic structure of surfactants, surfactants tend to be adsorbed onto the interfaces between air and water and between oil and water. Consequently, the property of surfactants has been widely applied to cleaning, wetting, dispersing, emulsifying, foaming, anti-foaming, and so on.

Proteins are biomolecules of great importance in the biochemical processes such as the medical, pharmaceutical, and food fields, since they exhibit their outstanding biological activities under mild conditions. However, proteins are easily denatured under unsuitable conditions such as heat and extreme pH in the process of separation, purification, storage, or enzymatic reaction, and the insoluble aggregate of denatured proteins tends to be formed. Additionally, when using recombinant DNA expression in bacteria such as Escherichia coli, insoluble inactive aggregated proteins, which are called inclusion bodies, are often formed [2]. Generally, in order to activate denatured proteins, it is first necessary to dissolve the aggregate of denatured proteins in aqueous solutions containing denaturants such as guanidine hydrochloride (GuHCl) and urea. Second, denatured proteins solubilized in aqueous solutions are refolded by diluting an aqueous solution of denatured proteins at a high dilution factor, while preventing dissolved proteins from aggregating, since the renaturation and aggregation processes compete in the process of refolding proteins [3]. In the dilution process, it is desirable that the amount of denaturants added to dissolve the aggregate of proteins is lesser as possible, since high protein concentrations should be kept in the process. From an industrial viewpoint, the reduction of the volume of solutions to be processed would reduce the processing scale, time, and cost. However, the refolding yield tends to decrease with an increase in the final concentration of proteins to be refolded.

Additives such as poly (ethylene glycol), salts, sugars, short chain alcohols, and surfactants have been used to effectively refold denatured proteins [3]. These additives bind critical interactive sites of denatured proteins, thereby preventing aggregation and/or misfolding. Especially, surfactants have potential upon the assistance of refolding because of various kinds of them. On the other hand, it has been well known that surfactants such as sodium dodecyl sulfate denature native proteins at high concentrations of surfactants, and are used in the measurement of electrophoresis [4].

In our previous work, we have reported that the waterin-oil (w/o) microemulsion of sucrose fatty acid esters depresses the aggregation of denatured HEWL, and forces denatured HEWL to be refolded [5]. In the w/o microemulsion system, the sufficient recovery efficiency and high refolding yield of renatured lysozyme are obtained. However, the productivity of refolded proteins per volume of w/o microemulsion system is limited due to low overall concentration of proteins in the w/o microemulsion system, since the volumetric ratio of water phase playing a role as the refolding field of proteins is too small. In the present work, we have addressed the question of how the dissolution ability of surfactants affects the refolding of proteins when the dilution method is carried out at the high final protein concentration without denaturants. We have employed hexadecyltrimethylammonium bromide (CTAB) as a surfactant and hen egg-white lysozyme (HEWL) as a model protein, since they are well investigated regarding their structures, functions, and properties [1,6].

2. Experimental

2.1. Materials

Lysozyme from hen egg whites (HEWL) (EC 3.2.1.17, 46400 units/mg solid, MW = 14300, pI = 11), Micrococcus lysodeikticus (ATCC No. 4698), and dithiothreitol (DTT) were obtained from Sigma-Aldrich Co. Hexadecyltrimethylammonium bromide (CTAB), ethylenediaminetetraacetic acid (EDTA), oxidized glutathione (GSSG), and guanidine hydrochloride (GuHCl) were purchased from Kanto Chemical Co., Inc. DK-SS (sucrose fatty acids of 99 wt% monoesters and 1 wt% diand triesters, fatty acid constituent consisting of 60 wt% stearic acid and 40 wt% palmitic acid) was supplied from Dai-Ichi Kogyo Seiyaku. Other reagents were commercially available and used without purification.

2.2. Denaturation and Dissolution of HEWL

The protein solution in 50mM Tris-HCl buffer at pH 8 containing 1 mM EDTA, 16 mg/L HEWL, 32 mM DTT, and a given amount of CTAB or DK-SS was incubated at 25˚C for 24 hours.

2.3. Refolding of Denatured HEWL

As a typical procedure, the buffer solution containing denatured HEWL, CTAB, and DTT was diluted by 50 mM Tris-HCl buffer at pH 8 containing GSSG, and was incubated at 25˚C for 24 hours. After dilution, the final concentrations of HEWL, CTAB, DTT, and GSSG were 1 mg/L, 0.88 mM, 2 mM, and 4 mM, respectively.

The aqueous solutions used in this study were acetate buffer solutions at pH 3.6 and 5.2, phosphate buffer solutions at pH 6 and 7, Tris-HCl buffer solution at pH 8, borate buffer solutions at pH 9 and 10. The concentration of buffer solution was prepared at 50 mM.

2.4. Measurement of Aggregation Ratio

The buffer solution containing aggregates of denatured HEWL was centrifuged at 4000 rpm for 10 min. After centrifugation, the supernatant was measured at 280 nm. The absorption coefficients of native and denatured HEWL were 2.63 and 2.37 mL/mg∙cm, respectively [7].

The aggregation ratio (A. R.) was defined as follows: A. R. (%) = 100 × ([initial concentration of HEWL] – [concentration of HEWL in supernatant after aggregation])/ [initial concentration of HEWL].

2.5. Measurement of Remaining Activity and Refolding Yield of HEWL

The activity of HEWL was determined as follows. After adding 100 μL of the aqueous solution containing HEWL to 3 mL of 50mM Tris-HCl buffer at pH 8 containing 200 mg/L Micrococcus lysodeikticus at 25˚C, the absorbance was continuously measured at 450 nm by UV/Vis. Bacterial lysis is a first order reaction. The lysis rate constant (k) was calculated from the relationship between the absorbance and the reaction time.

The remaining activity (R. A.) was defined as follows: R. A. = 100 × k (of denatured HEWL)/ko (of native HEWL).

The refolding yield (R. Y.) was defined as follows: R. Y. = 100 × k (of renatured HEWL)/ko (of native HEWL).

3. Results and Discussion

3.1. Dissolution of Aggregates of Denatured HEWL by Surfactants

In the conventional method of dissolving aggregates of denatured HEWL, denaturants such as guanidine hydrochloride (GuHCl) and urea have been widely used at high concentrations. Consequently, when refolding denatured proteins, the solution of proteins must be diluted at a high dilution factor. In the present work, we have employed surfactants instead of denaturants.

Figure 1 shows the relationship of aggregation ratio with surfactant concentration. Any aggregation was not observed when the concentration of CTAB was at 3.5 mM or over. On the other hand, the solution became transparent when the concentration of DK-SS reached 65 mM. CTAB is a typical cationic surfactant, while DK-SS is a nonionic surfactant. The result indicates that the electrostatic repulsion among protein-surfactant complexes consisting of denatured protein molecules and surfactant molecules enhance the dissolution of proteinsurfactant complexes. Consequently, we have used CTAB in the following experiments.

3.2. Denaturation Effect of DTT on Activity of HEWL

DTT reduces the disulfide bonds of protein molecules. When DTT is used with denaturants such as guanidine hydrochloride (GuHCl) and urea, the denaturation of proteins is promoted [3]. Likewise, when CTAB is used with DTT instead of denaturants, we have assessed the denaturation effect of CTAB on HEWL.

Figure 2 shows the time course of remaining activity

Figure 1. Effect of surfactant concentration on the aggregation ratio of HEWL. A Tris-HCl buffer solution (50 mM at pH 8) containing 16 mg/mL HEWL, 32 mM DTT, and a certain amount of CTAB or DK-SS was incubated at 25˚C for 24 hr.

Figure 2. Time course of remaining activity of HEWL. A Tris-HCl buffer solution (50 mM at pH 8) containing 16 mg/mL HEWL, 32 mM DTT, and 14 mM CTAB was incubated at 25˚C.

of HEWL with 32 mM DTT. When the incubation time reached 3 hr, the activity of HEWL was not detected in the presence of DTT, while that of HEWL was kept perfectly in the absence of DTT. The solution of HEWL was transparent during the incubation. The result indicates that CTAB itself does not affect the activity of HEWL at the present concentration, but CTAB dramatically influences the activity in the presence of DTT.

3.3. Time Course of Refolding Yield in Refolding of Denatured HEWL

The refolding of proteins using dilution method has been carried out by diluting the denatured protein solution to a low final refolded protein concentration (0.01 - 0.1 mg/mL) in order to inhibit the formation in the aggregate of proteins and achieve the refolding of proteins efficiently. However, higher final concentration after the refolding of proteins by dilution is desirable particularly in a large-scale process. In the present work, we have examined the dilution method at a high final refolded protein concentration (1 mg/mL).

Figure 3 shows the time course of refolding yield. The refolding yield increased with an increase in incubation time, and reached plateau at 24 hr. Any precipitation was not observed during the refolding. The time scale of refolding in the present method was similar to that with denaturants in the conventional method [8].

3.4. Effect of CTAB Concentration on Refolding of Denatured HEWL

The properties of protein-surfactant complex such as surface tension, rheology, solubilization, and so on are influenced by surfactant concentration [9]. In order to estimate the effect of CTAB concentration on the refolding of HEWL, we have examined the relation between CTAB concentration and the refolding yield of HEWL. As seen in Figure 4, the optimum concentration of CTAB was 0.88 mM. Below the optimum concentration, the protein solution became slightly turbid. The optimum

Figure 3. Time course of refolding yield of HEWL. A TrisHCl buffer solution (50 mM at pH 8) containing 1 mg/mL HEWL, 2 mM DTT, 4 mM GSSG, and 0.88 mM CTAB was incubated at 25˚C.

Figure 4. Effect of CTAB concentration on the refolding yield of HEWL. A Tris-HCl buffer solution (50 mM at pH 8) containing 1 mg/mL HEWL, 2 mM DTT, 4 mM GSSG, and a certain amount of CTAB was incubated at 25˚C for 24 hr.

concentration is around the critical micelle concentration (cmc) of CTAB (0.98 mM) [1]. In general, the solubility of hydrophobic solutes tends to be lower at less than cmc. The result indicates that the amount of CTAB adsorbed on HEWL is not enough to dissolve the protein-surfactant complexes separately at less than the optimum concentration of CTAB. On the contrary, the amount of CTAB molecules adsorbed on a protein molecule is too much over the optimum concentration, and surfactants prevent denatured proteins from refolding.

3.5. Effect of [GSSG]/[DTT] Concentration on Refolding of Denatured HEWL

The molar ratio of oxidizing agents to reducing agents is crucial for forming the disulfide bond of proteins accurately [3,8]. We have evaluated the optimum molar ratio ([GSSG]/[DTT]) by changing the concentration of GSSG at a constant concentration of DTT.

Figure 5 shows the plot of refolding yield against the concentration of GSSG. The refolding yield sharply increased with an increase in the concentration of GSSG, the maximum refolding yield was observed at 3 mM, and then the refolding yield gradually decreased. The optimum molar ratio of [GSSG] to [DTT] was 1.5.

3.6. Effect of Solution pH on Refolding of Denatured HEWL

The structure, function, and property of proteins are strongly dependent upon the solution pH [4]. In order to estimate the effect of solution pH on the refolding of denatured HEWL, we have measured the refolding yield at various pH values.

As shown in Figure 6, the refolding yield markedly depended upon solution pH, and the maximum refolding yield exhibited 80% at pH 5.2. As the isoelectric point (pI) of HEWL is 11, the overall charge of HEWL increases in a decrease in solution pH, indicating that the electrostatic repulsion among HEWL molecules increases. The electrostatic repulsion prevents denatured HEWL

Figure 5. Effect of GSSG concentration on the refolding yield of HEWL. A Tris-HCl buffer solution (50 mM at pH 8) containing 1 mg/mL HEWL, 2 mM DTT, 0.88 mM CTAB, and a certain amount of GSSG was incubated at 25˚C for 24 hr.

Figure 6. Effect of solution pH on the refolding yield of HEWL. A buffer solution (50 mM at appropriate pH) containing 1 mg/mL HEWL, 2 mM DTT, 4 mM GSSG, and 0.88 mM CTAB was incubated at 25˚C for 24 hr.

from aggregating. Since HEWL is stable in the range from pH 5 to 7, the maximum refolding yield was obtained in the pH range. At more acidic pH, HEWL was less stable.

4. Conclusion

We have demonstrated that CTAB prevented the formation and growth of aggregates of HEWL, and denatured HEWL was sufficiently refolded at a high final refolded concentration of HEWL. The refolding yield depended upon the concentration of CTAB, the molar ratio of [GSSG] to [DTT], and the solution pH. Especially, the electrostatic repulsion among surfactant-protein complexes was strengthened by the synergy among the charges of CTAB and HEWL molecules, and the denatured HEWL was highly refolded at the optimum pH. Since the final HEWL concentration obtained by the present method is ten to one hundred times greater than that by the conventional dilution method, the present refolding method would be encouraging for its choice in bioindustrial application for protein separation.

Acknowledgements

The authors thank Dai-Ichi Kogyo Seiyaku Co. Ltd. for kindly supplying DK-SS.

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NOTES

*Corresponding author.