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Journal of Nanomaterials
Volume 2015 (2015), Article ID 616879, 6 pages
Research Article

Horseradish Peroxidase-Carrying Electrospun Nonwoven Fabrics for the Treatment of o-Methoxyphenol

1College of Science, Dalian Ocean University, Dalian, Liaoning 116023, China
2College of Science, Dalian Nationalities University, Dalian 116600, China

Received 3 July 2014; Revised 7 September 2014; Accepted 21 September 2014

Academic Editor: Yuqin Wan

Copyright © 2015 Chao Pan 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.


The carboxyl-functionalized polystyrene (poly(styrene-co-methacrylic acid), PSMAA) nanofibers with average diameters of 250 ± 20 nm was prepared by electrospinning. PSMAA nanofibrous membrane were employed for immobilization of horseradish peroxidase (HRP) enzyme on the fibrous surface by a chemical method. The parameters about immobilizing HRP on the PSMAA nanofibers were studied and the influence on the activity of the HRP is discussed. This study showed that soap-free emulsion method is an ideal technology to modify the polystyrene surface and ultimately achieve enzyme immobilization on electrospun PSMAA nanofibers surfaces. Compared with free HRP, the acid-base stability, thermal stability, and storage stability of HRP were increased after the immobilization. The immobilized HRP maintained about 60% of its initial activity during a 20-day storage period. However, the free HRP maintained only 40% of its initial activity. The removal percentages of o-methoxyphenol (OMP) reached 80.2% after 120 min for immobilized HRP. These results suggest that the proposed scheme for immobilization of HRP has potential in industrial applications for the treatment of phenolic wastewater.

1. Introduction

Horseradish peroxidase (HRP) has been shown to be able to remove a variety of phenols and aromatic amines from aqueous solutions [13]. However, the main drawback of treating wastewater by free HRP is its instability. To overcome this shortcoming, immobilization of HRP has been developed as an effective method for the applications of HRP, since it offered many advantages, such as increasing the stability of HRP and being repeatedly used easily [4, 5].

Electrospinning, being a simple and economical way to immobilize enzymes in situ, has received more and more attention in the last decade [610]. The appealing prospects of using electrospun fibrous membranes (EFMs) for enzyme immobilization include their tunable sizes (from micro to nanometer diameters), controllable morphology, high surface-to-volume ratio, and compositional variance. Thus, EFMs are regarded as a suitable support for the immobilization of enzymes. Recently, an application of immobilized HRP by electrospinning for removal of environmental pollutants from contaminated water has been reported. For example, Niu and coworkers [4] fabricated a HRP-immobilized poly(d,l-lactide-co-glycolide) (PLGA) fibers membrane for degradation of pentachlorophenol (PCP), obtaining removal efficiency of 83%.

In preparations for enzyme membranes, it is difficult to get bulk active groups on the membrane surface. The traditional plasma surface physics modification [11, 12] is complex and fussy and it has only a low effect on increasing immobilization of enzymes. The chemical modification of electrospun fibers has been shown to be an effective immobilization method compared with the physics modification. For instance, there has been reported in immobilization procedures using chemical modification, which allows condensation reaction between the carboxyl groups on electrospun fibers and the side chain amino groups of enzyme molecules, leading to covalent bond formations between the fibrous surfaces and enzyme molecules [13]. The chemical binding for enzyme immobilization can be applied for the enzymes which do not adsorb onto the cationic matrix, and thus the matrix is used for immobilizing a wider range of enzyme species.

In this paper, poly(styrene-co-methacrylic acid) (PSMAA) random copolymer nanofibers, having carboxyl groups on the MAA, were prepared by a combination of the soap-free emulsion polymerization method and an electrospinning technique (Scheme 1), which were employed as solid support to HRP enzyme, and immobilized HRP was used to remove OMP from water. The morphology, chemical structure of the PSMAA nanofibers, and the enzymatic properties of the immobilized HRP were investigated. The degradation efficiency of OMP by immobilized HRP was assessed.

Scheme 1: Chemical route for synthesis of styrene-co-methacrylic acid copolymer and subsequent electrospinning nanofibers attachment of HRP.

2. Experimental

2.1. Materials

The materials were used without further purification. N,N-Dimethylformamide (DMF) and o-methoxyphenol were purchased from the Shanghai Chemical Co. (China). The ingredients of phosphate buffer solution (PBS), such as orthophosphoric acid, dibasic sodium phosphate, and potassium phosphate monobasic, were of analytical grade and used as received. Horseradish peroxidase (HRP), Coomassie Brilliant Blue (G250), bovine serum albumin (BSA, molecular mass: 67,000 Da), phenol, 4-aminoantipyrine, and pyrocatechol (1,2-dihydroxybenzene) were purchased from Sigma-Aldrich co., China. The water used in all experiments was prepared in a three-stage Millipore Milli-Q Plus 185 purification system (Richmond Scientific Ltd. Great Britain) and had a resistivity higher than 18.2 MΩ/cm.

The styrene (Sty) and methacrylic acid (MAA) monomers were purchased from the Lingfeng Chemical Co. (China). These chemicals were distilled under vacuum at 75°C before use.

2.2. Synthesis of Poly(styrene-co-methacrylic Acid)

A typical synthesis was as follows: first, both Sty and MAA were distilled under vacuum at 75°C. 25 mL Sty and 1.0 mL MAA were then mixed, and the mixture and 100 mL water were added into a three-mouth flask with condenser and mechanical stirrer. The mixture was stirred at a speed of 300 rpm and heated under a heater cover. After 5 min of boiling, 0.1 g potassium persulfate powder (Sinopharm Chemical Reagent Co., Ltd, China) as initiator was added from the side mouth and the polymerization continued for 1.5 hours. The whole reaction was completed within 1.5 hours, with a conversion in excess of 90% (measured by the method of [14]). The resulting latex was cooled to ambient temperature and filtered through cheesecloth. The coagulum was dried and weighed.

2.3. Fabrication of PSMAA Nanofibers

A 15 wt.% PSMAA solution was prepared by adding 1.5 g PSMAA powder to 8.5 mL DMF at room temperature with magnetic stirring until it finally became a viscous precursor solution. The solution was quickly loaded into a 5 mL syringe equipped with a steel needle with a tip diameter of 0.5 mm, whose tip was filed flat, which was connected to a high-voltage supply capable of generating voltage up to 30 kV. A copper wire-framed drum collection screen was placed at a horizontal distance of 15 cm from the tip of the needle. The copper wire drum was connected to a motor with two pulleys and rotated at a speed of 300 rpm. The feeding rate of the precursor solution was controlled at 1 mL/h using an automatic syringe pump so that a small drop was maintained at the capillary tip due to the surface tension of the solution. The solution on the tip of the needle was ejected under a strong electric field of the 20 KV, and the PSMAA fibers thus formed were dried initially for 5 h at 70°C under vacuum.

2.4. Immobilization of HRP

An appropriate amount of electrospun PSMAA nanofibrous membranes were immersed in 50 mL of BSA solution (1% wt) for about 1.5 h at 20°C in shakers while stirring continuously and then thoroughly washed with deionized water to remove the residue BSA. Subsequently, the pretreated membranes were submerged into 20 mL of the HRP solution (1 mg/mL in the PBS, pH 7.0) in a 25 mL beaker and shaken gently in an ice bath for the required time. Finally, the membranes were taken out and washed with the PBS until no protein was detected in the washings.

2.5. Determination of Immobilization Capacity

The concentration of HRP in the solutions was determined by the method of Bradford [15] based on the absorbance of Coumassie Brilliant Blue reagent at 595 nm by UV-Visible spectroscopy (U-4100, Hitachi Co., Ltd, Japan). The amount of the bound enzyme was calculated aswhere is the amount of HRP bound onto unit mass of nanofibrous membranes (mg/g), and are the initial and equilibrium HRP concentrations in the solution (mg/mL), is the volume of the HRP solution, and is the mass of the nanofibrous membrane.

2.6. Characterization

The PSMAA nanofibers morphology was examined using (S-3000N, Hitachi, Co., Ltd, Japan) scanning electron microscope (SEM). All samples were sputter coated with gold. Fourier transform infrared (FTIR) spectra (BRUKER IFS66/S Perkin-Elmer) were recorded using pressed KBr pellets over the wavenumber range of 4000–500 cm−1 at a resolution of 4 cm−1 to determine the PS and PSMAA.

2.7. Activity Measurements of HRP

The Worthington protocol was followed to calculate the activity of the HRP enzymes [15]. In this method, hydrogen peroxide (H2O2), 4-aminoantipyrene (4-AAP), and phenol were first mixed to form a colorless reagent and the HRP enzyme was immersed in the colorless reagent to catalyze the conversion of H2O2 to water, along with the conversion of the colorless dye to a red color (quinoneimine). The rate of color change was recorded by using UV-vis absorbance spectroscopy at 510 nm, and the increase of absorbance was translated into enzyme activity through the specific absorptivity of the chromogen ( = 7100 M−1 cm−1) [16]. The substrates used were 2.46 × 10−3 mol/L 4-AAP with 0.172 mol/L phenol and 1.76 × 10−3 mol/L H2O2. All measurements were in a PBS with a pH of 7.0. Each experiment was repeated three times.

2.8. Degradation Experiments

HRP-PSMAA (1 cm × 1 cm, total weight 20 ± 1 mg) membrane pieces were added one each to 10 mL solutions with the concentration of OMP at 8.06 × 10−4 mol/L; the molar ratio of the reaction between OMP and H2O2 was about 1 : 1. The reaction scheme was suggested as shown in Scheme 2 [17, 18].

Scheme 2

The mixture was incubated at °C and pH 6.0 under reciprocal agitation at 30 rounds per minute. For the purpose of terminating the HRP catalysis, 0.1 mL of 0.658 mol/L H3PO4 was added when sampling. The control experiment for free HRP was carried out in the same reactor using an equivalent amount of HRP. The OMP concentrations in the aqueous phase and on/in the HRP-PSMAA (washed by acetonitrile) were measured by a UV-vis spectrophotometer (U-4100, Hitachi Co., Ltd, Japan) at 470 nm. The amount of OMP degraded by HRP was calculated bywhereis the initial amount of OMP in solution and is the amount of OMP retained in solution. All experiments were carried out at °C.

3. Results and Discussion

3.1. FTIR Spectra of Copolymer

FTIR spectra of (a) the PS and (b) the PSMAA are shown in Figure 1; comparing these two spectra, the spectrum of the PSMAA membrane showed an absorbance band at 1698.97 cm−1, which is a characteristic band for carboxyl groups. It indicates that COOH groups of methacrylic acid have been blocked to styrene successfully.

Figure 1: FT-IR spectrum of PS and PSMAA.
3.2. The Surface Morphologies of the Nanofibrous Membrane

A SEM image of the original PSMAA nanofibers is displayed in Figure 2(a). The morphology of the nanofiber appears uniform, with the diameter of the nanofibers ranging from 230 to 270 nm. After HRP immobilization, as shown in Figure 2(b), the diameter and the morphology of the nanofibers did not change substantially, although some of adhesion between the fibers compared with that un-immobilized. It might be because the –COOH groups of the PSMAA nanofibrous membranes reacted with amine groups of HRP protein, the bound protein then acted as a seed, and other unbound HRP molecules were adsorbed on the bound protein to form protein aggregation by molecular interactions.

Figure 2: Morphologies of PSMAA nanofiber. (a) Original PSMAA nanofibers. (b) PSMAA nanofibers with immobilization of HRP.
3.3. Effect of Immobilization Time on Enzyme Capacity and Activity of HRP Immobilized on the PSMAA Nanofibers

To determine the optimum adsorption time, the effect of adsorption time on the immobilized amount of protein was studied. As shown in Figure 3, adsorption equilibrium was reached when the experiment running for 4 h and the activity of the immobilized HRP increased with prolonged coupling time, and the highest activity was obtained when immobilization was allowed to proceed for 4 h. However, the activity decreased if the reaction time was longer; this might be because the long time coupling reaction to change unfolding degree of the enzyme molecule, resulting in a enzyme conformation is destroyed, causing inactivation of the enzyme. Therefore, to ensure the maximum adsorption of HRP onto the membranes, the adsorption time was adopted as 4 h in the following experiments.

Figure 3: Effect of immobilization time on enzyme loading capacity at pH 7.0 and room temperature.
3.4. Effect of Temperature on the Activity of HRP

The effect of temperature on the activity of free and immobilized HRP at pH 7.0 is shown in Figure 4, the maximum activity of the free HRP appeared at 35°C, but the optimum temperature of the immobilized HRP was slightly higher at 40°C. At temperatures above 35°C, as the temperature increased, the residual activity of the free HRP decreased faster than that of the immobilized HRP; that is, the immobilized HRP exhibited higher heat resistance than the free one. This is suggested to be due to interactions between enzyme and the PSMAA-COOH supports that limited the enzyme movement to reduce the degree of freedom of the spatial structure of enzyme, protecting it from deactivation at high temperatures.

Figure 4: Effect of temperature on the activity of free and immobilized HRP.
3.5. Storage Stability

The storage stability of immobilized and free enzyme is presented in Figure 5 and the residual activity of immobilized and free HRP was 87.4% and 45.4% after 5 days, respectively. The results indicated that the storage stability of immobilized HRP was better than that of free HRP, which is suggested to be due to the immobilization of the enzyme limiting the freedom of conformational changes, resulting in increasing stability towards denaturalization [19].

Figure 5: Storage stability of free and immobilized HRP.
3.6. Effect of pH on the Activity of HRP

Figure 6 shows the effect of pH on the activity of the free and immobilized HRP. The optimal pH value was about 6.0 for both free and immobilized enzyme; no significant shift of the optimal pH was observed. But the residual relative activity of the immobilized HRP was higher than that of the free one at all other pH in the range between 2.0 and 9.0. The lower sensitivity of the immobilized enzyme to pH is probably because of a significant alteration of the enzyme microenvironment upon immobilization on the fibers.

Figure 6: Effect of pH on the activity of HRP.
3.7. o-Methoxyphenol (OMP) Removal by Free and Immobilized HRP

Figure 7 shows the efficiency of removal of OMP in a batch experiment running for 120 min. The removal process by PSMAA-HRP was fast and reached a removal percentage of about 80.2%. The removal efficiency of PSMAA-HRP was higher than free HRP. This is suggested to be due to the fact that the OMP removal by immobilized enzyme was the result of both PSMAA nanofibers adsorption and enzymatic catalyzation; the OMP molecules diffuse from the bulk solution to the external surfaces of the PMAA nanofibers and adsorb onto the easily accessible hydrophobic sites on the surface. In addition a great amount of OMP was degraded by the HRP which is immobilized on the surface of fibers, and this step is usually assumed to be a fast one.

Figure 7: Degradation kinetics of OMP by PSMAA, free HRP, and HRP-PSMAA.

4. Conclusion

PSMAA nanofibrous membranes with uniform fiber diameters between 230 and 270 nm were prepared by an electrospinning method. HRP enzyme was successfully immobilized on the MAA carboxyl groups of the PSMAA nanofibers. The results of degradation experiments indicated that a removal efficiency of 80.2% was achieved. Immobilized HRP showed a better acid-base stability, thermal stability, and storage stability than free HRP, which is a very attractive aspect for real applications involving a sufficiently wide range of external conditions.

Conflict of Interests

The authors declare that there is no conflict of interests regarding the publication of this paper.


The authors acknowledge the financial support of the National Natural Science Foundation (no. 21102033), the Open Research Fund of MOIDAT (no. 201205), the Open Research Fund of State Key Laboratory of Fine Chemicals (no. KF1012), the Open Project Program of Key Laboratory of Ecotextiles, Ministry of Education, Jiangnan University (no. KLET1205), and the Scientific Research Fund of Liaoning Provincial Education Department (no. L2011122).


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