Increased thermostability and phenol removal efficiency by chemical modified horseradish peroxidase

Horseradish peroxidase was modified by phthalic anhydride and glucosamine hydrochloride. The thermostabilities and removal efficiencies of phenolics by native and modified HRP were assayed. The chemical modification of horseradish peroxidase increased their thermostability (about 10- and 9-fold, respectively) and in turn also increased the removal efficiency of phenolics. The quantitative relationships between removal efficiency of phenol and reaction conditions were also investigated using modified enzyme. The optimum pH for phenol removal is 9.0 for both native and modified forms of the enzyme. Both modified enzyme could suffer from higher temperature than native enzyme in phenol removal reaction. The optimum molar ratio of hydrogen peroxide to phenol was 2.0. The phthalic anhydride modified enzyme required lower dose of enzyme than native horseradish peroxidase to obtain the same removal efficiency. Both modified horseradish peroxidase show greater affinity and specificity of phenol.     

Effect of reaction conditions on phenol removal by polymerization and precipitation using Coprinus cinereus peroxidase

The quantitative relationships between removal efficiency of phenol and reaction conditions were investigated using Coprinus cinereus peroxidase. The most effective ratio of hydrogen peroxide to phenol was nearly 1/1 (mol/mol) at an adequate enzyme dose. 12.2 U of the enzyme was needed to remove 1 mg of phenol when our peroxidase preparation was used. At an insufficient peroxidase dose, the optimum pH value was 9.0, and lowering the reaction temperature led to the improvement of removal efficiency. At an excess peroxidase dose, almost 100% removal of phenol was obtained over a wide range of pH (5-9) and temperature (0-60 degrees C). Despite the presence of culture medium components, it was shown that Coprinus cinereus peroxidase had the same phenol polymerization performance as horseradish peroxidase or Arthromyces ramosus peroxidase.     

Application of immobilized horseradish peroxidase onto modified acrylonitrile copolymer membrane in removing of phenol from water

A non-modified and modified with NaOH and ethylenediamine ultrafiltration membranes prepared from AN copolymer have been used as carriers for the immobilization of horseradish peroxidase (HRP) enzyme. The amount of bound protein onto the membranes and the activity of the immobilized enzyme have been investigated as well as the pH and thermal optimum, and the thermal stability of the free and immobilized HRP. The experiments have proved that the modified membrane is a better support for the immobilization of HRP enzyme. The latter has shown a greater thermal stability than the free enzyme.A possible application has been studied for reducing phenol concentration in water solutions through oxidation of phenol by hydrogen peroxide, in the presence of free and immobilized HRP enzyme on modified AN copolymer membranes. A higher degree of the phenol oxidation has been observed in the presence of the immobilized enzyme. A total removal of phenol has been achieved in the presence of immobilized HRP at concentration of the hydrogen peroxide 0.5 mmol L^?1 and concentration of the phenol in the model solutions within the interval 5–40 mg L^?1. A high degree of phenol oxidation (95.4%) has been achieved in phenol solution with 100 mg L^?1 concentration in the presence of hydrogen peroxide and immobilized HRP, which demonstrates the promising opportunity of using the enzyme for bioremediation of waste waters, containing phenol.The immobilized HRP has shown good operational stability. Deactivation of the immobilized enzyme to 50% of the initial activity has been observed after the 20th day of the enzyme operation.     

Structural change and catalytic activity of horseradish peroxidase in oxidative polymerization of phenol

The effects of solvent and reaction conditions on the catalytic activity of horseradish peroxidase (HRP) were investigated for oxidative polymerization of phenol in water/organic mixtures using hydrogen peroxide as an oxidant. Also, the structural changes of HRP were investigated by CD and absorption spectroscopy in these solvents. The results suggest that the yield of phenol polymer (the conversion of phenol to polymer) is strongly affected by the reaction conditions due to the structural changes of HRP, that is, the changes in higher structure of the apo-protein and dissociation or decomposition of the prosthetic heme. Optimum solvent compositions for phenol polymerization depend on the nature of the organic solvents owing to different effects of the solvents on HRP structure. In addition to initial rapid changes, slower changes of HRP structure occur in water/organic solvents especially at high concentrations of organic solvents. In parallel with these structural changes, catalytic activity of HRP decreases with time in these solvents. At higher reaction temperatures, the yield of the polymer decreases, which is also ascribed to modification of HRP structure. It is known that hydrogen peroxide is an inhibitor of HRP, and the yield of phenol polymer is strongly dependent on the manner of addition of hydrogen peroxide to the reaction solutions. The polymer yield decreases significantly when hydrogen peroxide was added to the reaction solution in a large amount at once. This is probably due to inactivation of HRP by excess hydrogen peroxide. From the CD and absorption spectra, it is suggested that excess hydrogen peroxide causes not only decomposition of the prosthetic heme but also modification of the higher structure of HRP.     

Structural Change and Catalytic Activity of Horseradish Peroxidase in Oxidative Polymerization of Phenol

The effects of solvent and reaction conditions on the catalytic activity of horseradish peroxidase (HRP) were investigated for oxidative polymerization of phenol in water/organic mixtures using hydrogen peroxide as an oxidant. Also, the structural changes of HRP were investigated by CD and absorption spectroscopy in these solvents. The results suggest that the yield of phenol polymer (the conversion of phenol to polymer) is strongly affected by the reaction conditions due to the structural changes of HRP, that is, the changes in higher structure of the apo-protein and dissociation or decomposition of the prosthetic heme. Optimum solvent compositions for phenol polymerization depend on the nature of the organic solvents owing to different effects of the solvents on HRP structure. In addition to initial rapid changes, slower changes of HRP structure occur in water/organic solvents especially at high concentrations of organic solvents. In parallel with these structural changes, catalytic activity of HRP decreases with time in these solvents. At higher reaction temperatures, the yield of the polymer decreases, which is also ascribed to modification of HRP structure. It is known that hydrogen peroxide is an inhibitor of HRP, and the yield of phenol polymer is strongly dependent on the manner of addition of hydrogen peroxide to the reaction solutions. The polymer yield decreases significantly when hydrogen peroxide was added to the reaction solution in a large amount at once. This is probably due to inactivation of HRP by excess hydrogen peroxide. From the CD and absorption spectra, it is suggested that excess hydrogen peroxide causes not only decomposition of the prosthetic heme but also modification of the higher structure of HRP.     

A model of peroxidase activity with inhibition by hydrogen peroxide

The rate of color formation in an activity assay consisting of phenol and hydrogen peroxide as substrates and 4-aminoantipyrine as chromogen is significantly influenced by hydrogen peroxide concentration due to its inhibitory effect on catalytic activity. A steady-state kinetic model describing the dependence of peroxidase activity on hydrogen peroxide concentration is presented. The model was tested for its application to soybean peroxidase (SBP) and horseradish peroxidase (HRP) reactions based on experimental data which were measured using simple spectrophotometric techniques. The model successfully describes the dependence of enzyme activity for SBP and HRP over a wide range of hydrogen peroxide concentrations. Model parameters may be used to compare the rate of substrate utilization for different peroxidases as well as their susceptibility to compound III formation. The model indicates that SBP tends to form more compound III and is catalytically slower than HRP during the oxidation of phenol.     

Effect of temperature and pH on phenol removal using purified Coprinus cinereus peroxidase

The removal of phenol by peroxidase-catalysed polymerization was examined using purified Coprinus cinereus peroxidase. The phenol removal efficiency increased with a decrease in the reaction temperature over the range of 0–70 °C, though only a trace of enzyme activity with 4-aminoantipyrine (4-AAP), phenol and hydrogen peroxide was found at 0 °C. The optimum pH value for phenol removal was 9.0, while the enzyme expressed maximum activity at pH 7.5 in the presence of 4-AAP, phenol and hydrogen peroxide. By measuring residual enzyme activity in the polymerizing reaction mixture, it was shown that enzyme inactivation by free radicals was more suppressed at 0 °C than at 40 °C and that the adsorption of the enzyme on the polymerized precipitate was more suppressed at pH 9.0 than that at pH 7.5.     

Peroxidase-catalyzed color removal from bleach plant effluent

Effluent from the caustic extraction stage of a bleach plant is highly colored due to the presence of dissolved products from lignin chlorination and oxidation. Color removal from the effluent by hydrogen peroxide at neutral pH was catalyzed by addition of horseradish peroxidase. The catalysis with peroxidase (20 mg/L) was observed over a wide range of peroxide concentrations (0.1mM-500mM), but the largest effect was between 1mM and 100mM. The pH optimum for catalysis was around 5.0, while the basal rate of noncatalyzed peroxide color removal simply increased with pH within the range tested (3-10). Peroxidase catalysis at pH 7.6 reached a maximum at 40 degrees C in 4 h assays with 10mM peroxide, and disappeared above 60 degrees C. Compared with mycelial color removal by Coriolus versicolor, the rate of color removal by peroxide plus peroxidase was initially faster (first 4 h), but the extent of color removal after 48 h was higher with the fungal treatment. Further addition of peroxidase to the enzyme-treated effluent did not produce additional catalysis. Thus, the peroxide/peroxidase system did not fully represent the metabolic route used by the fungus.     

An enzymatic method for removal of phenol from industrial effluent

Phenols in an aqueous solution were removed after treatment with peroxidase in the presence of hydrogen peroxide. Phenols occur in wastewater of a number of industries, such as high temperature coal conversion, petroleum refining, resin and plastic, wood and dye industries, etc. It can be toxic when present at elevated levels and is known to be carcinogeneous. Thus, removal of such compound from these industrial effluents is of great importance. An enzymatic method for removal of phenols from industrial wastewater, using turnip peroxidase, has been developed. Phenol-containing industrial wastewater was treated with immobilized turnip peroxidase in the presence of hydrogen peroxide. In the reaction, a number of phenols are oxidized to form the corresponding free radicals in the presence of hydrogen peroxide as an oxidant. Free radicals polymerize to form substances that are less soluble in water than the original substances. The precipitates were removed by conventional methods and residual phenol was estimated. The present report describes the immobilization of turnip peroxidase on silica via covalent coupling, and its utility in phenol removal. A comparative study was also carried out with other immobilization techniques, viz., calcium alginate entrapment, polyacrylamide gel entrapment, etc. Peroxidase, covalently bound to silica, showed 95% removal of phenol, whereas naphthol was removed up to 99%.     

Functional expression and stabilization of horseradish peroxidase by directed evolution in Saccharomyces cerevisiae

Biotechnology applications of horseradish peroxidase (HRP) would benefit from access to tailor-made variants with greater specific activity, lower K(m) for peroxide, and higher thermostability. Starting with a mutant that is functionally expressed in Saccharomyces cerevisiae, we used random mutagenesis, recombination, and screening to identify HRP-C mutants that are more active and stable to incubation in hydrogen peroxide at 50 degrees C. A single mutation (N175S) in the HRP active site was found to improve thermal stability. Introducing this mutation into an HRP variant evolved for higher activity yielded HRP 13A7-N175S, whose half-life at 60 degrees C and pH 7.0 is three times that of wild-type (recombinant) HRP and a commercially available HRP preparation from Sigma (St. Louis, MO). The variant is also more stable in the presence of H(2)O(2), SDS, salts (NaCl and urea), and at different pH values. Furthermore, this variant is more active towards a variety of small organic substrates frequently used in diagnostic applications. Site-directed mutagenesis to replace each of the four methionine residues in HRP (M83, M181, M281, M284) with isoleucine revealed no mutation that significantly increased the enzyme's stability to hydrogen peroxide.     

Dephenolization of industrial wastewaters catalyzed by polyphenol oxidase

A new enzymatic method for the removal of phenols from industrial aqueous effluents has been developed. The method uses the enzyme polyphenol oxidase which oxidizes phenols to the corresponding o-quinones; the latter then undergo a nonenzymatic polymerization to form water-insoluble aggregates. Therefore, the enzyme in effect precipitates phenols from water. Polyphenol oxidase has been found to nearly completely dephenolize solutions of phenol in the concentration range from 0.01 to 1.0 g/L. The enzymatic treatment is effective over a wide range of pH and temperature; a crude preparation of polyphenol oxidase (mushroom extract) is as effective as a purified, commercially obtained version. In addition to phenol itself, polyphenol oxidase is capable of precipitating from water a number of substituted phenols (cresols, chlorophenols, naphthol, etc.). Also, even pollutants which are unreactive towards polyphenol oxidase can be enzymatically coprecipitated with phenol. The polyphenol oxidase treatment has been successfully used to dephenolize two different real industrial waste-water samples, from a plant producing triarylphosphates and from a coke plant. The advantage of the polyphenol oxidase dephenolization over the peroxidase-catalyzed one previously elaborated by the authors is that the former enzyme uses molecular oxygen instead of costly hydrogen peroxide (used by peroxidase) as an oxidant.     

Magnetite-supported hematin as a biomimetic of Horseradish peroxidase in phenol removal by polymerization

Phenol removal using HRP and hematin as a biomimetic of HRP has been studied under various conditions at room temperature. The best results were obtained with treatment in two steps, with double addition of HRP or hematin and a final treatment with activated carbon. This two-step treatment achieved a minimum of 90% conversion of the initial phenol, under conditions commonly found in wastewaters (from 400 up to 1500 ppm phenol). Other additives such as chitosan, cellulose or polyethylene glycol (PEG) gave no satisfactory results.

Hematin and magnetite-supported hematin showed comparable activities in phenol removal from aqueous solution. The supported hematin is an interesting alternative to HRP for practical application of a biomimetic catalyst for phenol removal.     

Removal of pentachlorophenol by immobilized horseradish peroxidase

Researches on the polymerization of aqueous pentachlorophenol (PCP) by the catalysis of horseradish peroxidase (HRP) with the existence of hydrogen peroxide (H₂O₂) were conducted. Factors, such as acidity, temperature, enzyme activity, and initial concentration of PCP and H₂O₂ that could influence the degradation were studied. Results showed that the optimum pH value for free enzyme was 5–6; relative higher temperature could accelerate the reaction greatly; PCP removal increased with an increase of enzyme concentration, and PCP (initial concentration 12.6 mg/L) removal percentage could reach nearly 70% under the highest enzyme concentration (about 0.05 u/ml) adopted in the experiment; removal percentage increased slightly with an increase of initial concentration of PCP, and when initial PCP concentrations were 13.0 and 0.7 mg/L, the removal percentages were about 73.7% and 35.7%, respectively; the molar ratio of the reaction between PCP and H₂O₂ was about 1:2.Based on the above results, researches on the removal of PCP by the immobilized HRP were conducted. The free HRP was immobilized on the polyacrylamide gel prepared by gamma-ray radiation method; then the immobilized HRP was filled into a column, and PCP was successfully removed by the immobilized HRP column. The results were compared with results using free HRP enzyme, which showed that the optimum pH value for the immobilized HRP is similar to that for the free HRP, and when pH=5.15, the immobilized HRP could reduce PCP with initial concentration 13.4 mg/L to the concentration of 4.9 mg/L within 1 h, and the immobilized HRP column could be used to repeatedly.     

Determination of hydrogen peroxide generated by reduced nicotinamide adenine dinucleotide oxidase

Hydrogen peroxide can be conveniently determined using horseradish peroxidase (HRP) and 2,2'-azino-bis(3-ethylbenzthiazoline-6-sulfonic acid). However, interference occurs among assay components in the presence of reduced nicotinamide adenine dinucleotide (NADH) that is also a substrate of NADH oxidase. So, depletion of NADH is required before using the HRP method. Here, we report simple and rapid procedures to accurately determine hydrogen peroxide generated by NADH oxidase. All procedures developed were based on the extreme acid lability of NADH and the stability of hydrogen peroxide, because NADH was decomposed at pH 2.0 or 3.0 for 10 min, while hydrogen peroxide was stable at pH 2.0 or 3.0 for at least 60 min. Acidification and neutralization were carried out by adjusting sample containing NADH up to 30 microM to pH 2.0 for 10 min before neutralizing it back to pH 7.0. Then, hydrogen peroxide in the sample was measured using the HRP method and its determination limit was found to be about 0.3 microM. Alternatively, hydrogen peroxide in samples containing NADH up to 100 microM could be quantitated using a modified HRP method that required an acidification step only, which was found to have a determination limit of about 3 microM hydrogen peroxide in original samples.     

Immobilisation of soybean seed coat peroxidase on its natural support for phenol removal from wastewater

Soybean seed coat peroxidase (SBP; EC 1.11.1.7) was immobilised on its natural support, soybean seed coats, anticipating its use in phenol removal. Periodate and glutaraldehyde chemistries were assayed. Periodate failed to immobilise any SBP, whereas glutaraldehyde was effective. The optimum concentration of glutaraldehyde was found to be 1%. Immobilisation shifted the optimum pH for phenol removal from 4.0 to 6.0. Treated seed coat retained its activity over a 4-week period, and reusability assays showed that treated seed coats could be reused once for phenol removal. Polyethylene glycol (PEG) increased the stability of phenol degradation activity. In addition, the phenolic polymer was adsorbed on to seed coats, thus making removal of the polymeric product easier.     

Immobilisation of soybean seed coat peroxidase on its natural support for phenol removal from wastewater

Soybean seed coat peroxidase (SBP; EC 1.11.1.7) was immobilised on its natural support, soybean seed coats, anticipating its use in phenol removal. Periodate and glutaraldehyde chemistries were assayed. Periodate failed to immobilise any SBP, whereas glutaraldehyde was effective. The optimum concentration of glutaraldehyde was found to be 1%. Immobilisation shifted the optimum pH for phenol removal from 4.0 to 6.0. Treated seed coat retained its activity over a 4-week period, and reusability assays showed that treated seed coats could be reused once for phenol removal. Polyethylene glycol (PEG) increased the stability of phenol degradation activity. In addition, the phenolic polymer was adsorbed on to seed coats, thus making removal of the polymeric product easier.     

Purification, characterization and evaluation of extracellular peroxidase from two Coprinus species for aqueous phenol treatment

Non-ligninolytic fungal peroxidases produced by Coprinus cinereus UAMH 4103 and Coprinus sp. UAMH 10067 were purified, characterized and evaluated as cost-effective alternatives to horseradish peroxidase for aqueous phenol treatment. Purified Coprinus peroxidases exhibited a molecular weight of 36 kDa on matrix-assisted laser desorption ionization time-of-flight mass spectrometry. Although the catalytic properties of the two Coprinus peroxidases were nearly identical in both crude and purified forms, the stabilities were substantially different. The peroxidase from Coprinus sp. UAMH 10067 was more stable at 50 degrees C and under basic conditions (up to pH 10) than the enzyme from C. cinereus UAMH 4103. The former enzyme also performed better at pH 9 than the latter one in aqueous phenol treatment. The phenol removal efficiency of the Coprinus peroxidase was comparable to those of previously studied plant peroxidases. The broader working pH and higher thermal and alkaline stability of the peroxidase from Coprinus sp. UAMH 10067 may be advantageous for its application to industrial wastewater treatment.     

A comparative study of free and immobilized soybean and horseradish peroxidases for 4-chlorophenol removal: protective effects of immobilization

Horseradish peroxidase (HRP) and soybean peroxidase (SBP) were covalently immobilized onto aldehyde glass through their amine groups. The activity yield and the protein content for the immobilized SBP were higher than for the immobilized HRP. When free and immobilized peroxidases were tested for their ability to remove 4-chlorophenol from aqueous solutions, the removal percentages were higher with immobilized HRP than with free HRP, whereas immobilized SBP needs more enzyme to reach the same conversion than free enzyme. In the present paper the two immobilized derivatives are compared. It was found that at an immobilized enzyme concentration in the reactor of 15 mg l(-1), SBP removed 5% more of 4-chlorophenol than HRP, and that a shorter treatment was necessary. Since immobilized SBP was less susceptible to inactivation than HRP and provided higher 4-chlorophenol elimination, this derivative was chosen for further inactivation studies. The protective effect of the immobilization against the enzyme inactivation by hydrogen peroxide was demonstrated.     

Peroxidase Oxidation of Phenols

Partially purified preparations of horseradish peroxidase were able to catalyze the effective transformation of such phenol compounds as phenol, o-chlorophenol, 2,4,6-trichlorophenol, pentachlorophenol (giving rise to the formation of polymer products insoluble in water), resorcinol, and thymol (giving rise to the formation of low-molecular-weight products). The following conditions were found to be optimal for peroxidase oxidation and provide the maximum extent of elimination of phenol compounds: temperature, 15–25 and 25–30°C for phenol and chlorophenol compounds, respectively; molar ratio H₂O₂/phenol, 1 : 1; and transformation time, 1–3 h. Although effective transformation was observed within a broad range of pH, the efficiency of the process slightly increased at a pH from 6.0 to 7.5. It was suggested to carry out multiple peroxidase oxidations of phenols using partially purified peroxidase enclosed in a dialysis membrane bag placed into a solution of a phenol compound containing hydrogen peroxide.     

Biocatalytic properties of recombinant tobacco peroxidase in chemiluminescent reaction

The wild-type anionic tobacco peroxidase and its Glu141Phe mutant have been expressed in Escherichia coli, and reactivated to yield active enzymes. A Glu141Phe substitution was made with the tobacco anionic peroxidase (TOP) to mimic neutral plant peroxidases, such as horseradish peroxidase (HRP). Both recombinant forms of tobacco peroxidase show extremely high activity in luminol oxidation with hydrogen peroxide, and thus, preserve the unique property of the native tobacco peroxidase, a superior chemiluminescent reagent. The chemiluminescent signal intensity for both recombinant forms of TOP is orders of magnitude higher than that for wild-type recombinant HRP. The substitution slightly increases TOP activity and stability in the reaction course, but has almost no effect on the optimal parameters of the reaction (pH, luminol and hydrogen peroxide concentrations) and calibration plot. Comparison of substrate specificity profiles for recombinant TOP and HRP demonstrates that Glu141 has no principal effect on the enzyme activity. It is not the presence of the negative charge at the haem edge, but the high redox potential of TOP Compounds I and II that provides high activity towards aromatic amines and aminophenols, and luminol in particular.