PROCESS FOR PRODUCING PEROXIDASE

Abstract: A novel peroxidase was obtained from a fast growing microorganism of the genus Coprinus cinereus. The fungal peroxidase is comparable to the conventional peroxidase de­ rived from horseradish or Japanese radish in that it can be used either as a clinical or diagnostic reagent or as a marker enzyme in enzyme immunoassay.

Description: The present invention relates to a process for producing a peroxidase using a microorganism. More particularly, the invention relates to a process for producing a peroxidase that is produced by a fungi of the genus Coprinus of the basidiomycetes and which develops color with the aid of a hydrogen donor such as a 4-amino-antipyrine (hereunder abbreviated as 4-AA)-phenol system, a 3-methyl-2-benzothiazolinone hydrazone (hereunder MBTH)-diethylaniline (hereunder DEA) system, and a 2,2'-azino-di(3-ethylbenzothiazoline)-6-sulfonic acid (hereunder ABTS). Peroxidase is an enzyme that oxidizes a variety of compounds in the presence of hydrogen peroxide. Currently, peroxidase is used as a clinical or diagnostic reagent in combination with a variety of oxidases for the assay of glucose, cholesterol, phospholipids and uric acid. Another current use of peroxidase is as a marker enzyme in enzyme immunoassay. Commercially available sources of peroxidase are plants such as horseradish and Japanese radish. Since the peroxidase originating from such plants contains isozymes of slightly different properties, they must be separated laboriously in order to obtain a pure form of peroxidase suitable for use as a diagnostic reagent. Peroxidases originating from microorganisms are also known and they include Cytochrome C peroxidase and NADH peroxidase produced from bacteria and fungi. However, these peroxidases are not non-specific as are the ordinary peroxidases derived from horseradish and Japanese radish, and such peroxidases specific to a particular system are not suitable for use as clinical and diagnostic reagents. It has recently been reported that peroxidase using o-dianisidine as a hydrogen donor can be produced from E. coli or microorganisms of the genus Myrothecium . However, this peroxidase is also unsuitable as a diagnostic reagent since the use of o-dianisidine in clinical and diagnostic agents is increasingly discouraged because of its potential carcinogenic effects. Nyunoya et al, J. Gen. Appl. Microbiol., 26, 229-238 (1980) teach that Coprinus macrorhizus produces an "intracellular peroxidase". It is the object of the present invention to obtain from fast growing microorganisms a peroxidase that is comparable to the conventional peroxidase derived from horseradish or Japanese radish in that it can be used either as a clinical or diagnostic reagent or as a marker enzyme in enzyme immunoassay. This object is achieved by a process for producing a peroxidase, comprising the steps of culturing Coprinus cinereus and recovering the peroxidase secreted by cells in the culture. To attain this object, the inventors isolated a large number of naturally occurring microorganisms and examined their ability to produce peroxidase that develops color with the aid of a hydrogen donor such as a 4-AA-phenol system, MBTH-DEA system or ABTS. As a result, the inventors found a fungal strain of the genus Coprinus that is capable of producing a peroxidase in a high yield. The present invention has been accomplished on the basis of this finding. Fig. 1 is a graph showing the relationship between the reaction pH and the relative activity of the peroxidase of the present invention; Fig. 2 is a graph showing the relationship between the reaction temperature and the relative activity of the peroxidase; Fig. 3 is a graph showing the pH stability of the peroxidase; and Fig. 4 is a graph showing the temperature stability of the peroxidase. Examples of microorganisms of the genus Coprinus that have the ability to produce peroxidase include Coprinus cinereus f. microsporus IFO 8371, C. cinereus f. microsporus IFO 30114, C. cinereus f. microsporus IFO 30627, C. cinereus f. microsporus IFO 30628 and C. cinereus f. microsporus IFO 31333, all being stored at the Institute for Fermentation, Osaka, Japan. Coprinus cinereus used in the present invention may be cultured by inoculating a liquid or solid medium with spores or mycelia from the strain or a liquid seed culture obtained by precultivation. A liquid medium may contain any common carbon sources such as glucose, fructose, xylose, saccharose, maltose, soluble starch, molasses, glycerol and mannitol. Usable nitrogen sources include naturally occurring substances such as peptone, yeast extract, malt extract, meat extract, casamino acids, and corn steep liquor, as well as organics such as urea, and inorganics such as sodium nitrate and ammonium nitrate. Inorganic salts (e.g. phosphates, magnesium sulfate, iron sulfate and copper sulfate) and vitamins may optionally be used as trace nutrient sources. Any of these components may be incorporated in a medium in any concentration that will not be detrimental to the growth of the microorganism of interest. For practical purposes, carbon sources are generally used in concentrations ranging from 0.1 to 10 wt%, preferably from 1 to 5 wt%, while nitrogen sources are in the range of 0.01 to 5 wt%, preferably 0.1 to 2 wt%. The cultivation temperature ranges from 10 to 42 o C, preferably from 30 to 37 o C. The medium is adjusted to a pH value in the range of 4 - 10, preferably 6 - 9, and cultivation is conducted by agitation culture under aeration, shake culture or stationary culture, for a period which generally lasts 3 to 14 days. A solid medium may be prepared from wheat bran, rice hulls, rice bran or any other suitable materials that are mixed with 50 - 100 wt% of water. Cultivation is carried out at temperatures between 10 and 42 o C, preferably between 30 and 37 o C, for a period of 3 - 14 days. If necessary, the medium may be supplemented with suitable nitrogen sources, inorganic salts or trace nutrient sources. For mass cultivation, a liquid medium is preferred. The culture obtained by the procedures described above has peroxidase accumulated therein. The term "culture" used here means either, the culture supernatant, the mixture of cells and culture supernatant or a culture filtrate if a liquid medium is used; if a solid medium is used, the term "culture" means the mixture of the cells and the medium on which they have grown. For example, if a liquid medium is used, peroxidase may be recovered from the culture mixture by the following procedures. When the full growth of the organism is attained, the culture mixture is subjected to a suitable solid-liquid separation means such as centrifugation or filtration, so as to obtain a crude enzyme solution free from the cells and insoluble matter. If cultivation is performed on a solid medium, a crude enzyme solution may be obtained by the following procedures: water is added to the solid medium containing the cultured cells, and any insoluble matter is removed from the mixture. A pure form of peroxidase may be isolated from the crude enzyme solution by conventional enzyme purification techniques, such as organic solvent fractionation, ammonium sulfate fractionation, dialysis, isoelectric precipitation and column chromatography, which may be used either independently or in combination. The activity of the peroxidase in accordance with the present invention may be determined by the following method, wherein a 4-AA-phenol system, for example, is used as a hydrogen donor. First, 1.3 ml of 0.1% phenol solution, 0.25 ml of 0.2% 4-AA solution and 0.2 ml of 0.02% hydrogen peroxide solution are added to 1 ml of 0.1M phosphate buffer (pH, 7.0) and the mixture is prewarmed to 37 o C. To the prewarmed mixture, 0.25 ml of a specific enzyme solution is added and subjected to reaction for 10 minutes. After the reaction, 0.2 ml of 20% sodium azide solution is added and the absorbance of the mixture is measured at 500 nm to obtain a reaction value, which is compared with a control value obtained by the same procedure except that the hydrogen peroxide solution is replaced by an equal volume (0.2 ml) of water. One unit (U) of peroxidase activity is indicated as the amount of oxygen that oxidizes 1 micromole of 4-AA-phenol per minute. The activity (U/ml) of peroxidase in an enzyme solution or culture solution is determined by the formula: 0.198 x 0.D.₅₀₀ x (the dilution rate of the enzyme or culture solution), wherein 0.D.₅₀₀ is the absorbance value after subtracting the control value. The peroxidase obtained by the present invention has the following properties. (1) Enzyme action: The peroxidase in accordance with the present invention catalyzes the oxidation of various compounds in the presence of hydrogen peroxide by the mechanism shown below: (wherein AH₂ is a hydrogen donor, and A is an oxidized hydrogen donor). (2) Specificity for hydrogen donor: The specificity of the peroxidase for a variety of hydrogen donors is shown in Table 1. H₂ donor Activity H₂ donor Activity Phenol +++ Hydroquinone + Pyrogallol +++ p-hydroxybenzoic acid ++ p-anisidine ++ p-aminobenzoic acid + o-dianisidine +++ ABTS +++ Guaiacol ++ Diethylaniline ± (3) Optimum pH: The optimum pH range at which the peroxidase exhibits the highest activity was checked by using samples having the same formulation as used for the assay of peroxidase activity in above (1), except that different buffers were used for different pH ranges: 0.1M acetate buffer for pH 3.5 - 5.5, 0.1M phosphate buffer for pH 5.5 - 8.0, 0.1M tris-HCl buffer for pH 7.5 - 9.0, and 0.1M glycine-sodium hydroxide buffer for pH 8.5 - 9.0. The results are summarized in Fig. 1. (4) Optimum working temperature: The activity of the peroxidase was measured over the temperature range of 10 - 90 o C, and the results are shown in Fig. 2. (5) pH stability: Different buffers were used for different pH ranges: 0.1M acetate buffer for pH 3.5 - 5.0, 0.1M phosphate buffer for pH 6.0 - 8.0, 0.1M tris-HCl buffer for pH 8.0 - 9.0, and 0.1M glycine-NaOH buffer for pH 9.0 - 12.0. To 0.9 ml of a specific buffer solution was added 0.1 ml of the peroxidase solution and the mixture was left to stand at 30 o C for 16 hours. The so treated enzyme solution was diluted 10-fold with 0.02M phosphate buffer (pH, 7.0) and the activity of the enzyme was measured. The results are shown in Fig. 3. (6) Temperature stability: Samples each prepared by adding 0.1 ml of the enzyme solution to 1.9 ml of 0.02M phosphate buffer (pH, 7.0) were held at varying temperature (10 - 90 o C) for 30 minutes. Immediately thereafter, the samples were cooled with iced water for 10 minutes and the residual enzyme activity in each sample was measured. The results are shown in Fig. 4. The following Examples are provided for further illustration of the invention. Example 1 Ten milliliters of a medium (pH, 6.0) containing 1% glucose, 0.5% polypeptone, and 0.3% yeast extract was put into a test tube having a diameter of 24 mm, and sterilized at 120 o C for 15 minutes. The sterilized medium was inoculated with a platinum loop of Coprinus cinereus IFO 8371, which was shake-cultured on a recipro-shaker (300 rpm) at 30 o C for 6 days. The culture mixture was filtered and the titer of peroxidase in the filtrate was found to be 1.3 U/ml. Example 2 Coprinus cinereus IFO 30627 was cultured for 7 days as in Example 1 and the filtrate of the culture had a peroxidase activity of 3.4 U/ml. Example 3 A medium (100 ml) of the same composition as that used in Example 1 was charged into a 500-ml Erlenmeyer flask and sterilized at 120 o C for 20 minutes. The sterilized medium was inoculated with a platinum loop of Coprinus cinereus IFO 30628 and shake-cultured on a recipro-shaker (110 rpm) at 34 o C for 6 days. The culture mixture was filtered and the titer of peroxidase in the filtrate was found to be 1.7 U/ml.

Claims: A process for producing a peroxidase, comprising the steps of culturing Coprinus cinereus and recovering the peroxidase secreted by cells in the culture. A process according to Claim 1, wherein the microorganism is cultured in a solid medium. A process according to Claim 1, wherein the microorganism is cultured in a liquid medium. A process according to Claim 1, wherein the culture medium contains 0.1 to 10 wt% of carbon sources selected from glucose, fructose, xylose, saccharose, maltose, soluble starch, molasses, glycerol and mannitol; 0.01 to 5 wt% of nitrogen sources selected from peptone, yeast extract, malt extract, meat extract, casamino acids, corn steep liquor, urea, sodium nitrate and ammonium nitrate; and a growth supporting amount of inorganic salts selected from phosphate, magnesium sulfate, iron sulfate and copper sulfate. A process according to Claim 1, wherein the culture is carried out at a temperature of between 10 and 42 o C and at a pH between 4 and 10 for 3 to 14 days. A process according to Claim 1, wherein the microorganism is selected from Coprinus cinereus f. microsporus IFO 8371, Coprinus cinereus f. microsporus IFO 30114, Coprinus cinereus f. microsporus IFO 30627, Coprinus cinereus f. microsporus IFO 30628 and Coprinus cinereus f. microporus IFO 31333.

Inventors: AMACHI, TERUO, AMANO, NORIHIDE, ASAMI, SUMIO, SHINMEN, YOSHIFUMI, YOSHIZUMI, HAJIME
Applicants: SUNTORY LIMITED
Application year: 1985
Main classification: C12N9
IPC codes: C12Q1, C12R1, C12N9