ENZYME AND PROCESS FOR ITS MANUFACTURE

Abstract: The novel coenzyme independent L-sorbosone dehydro­ genase, preferably originating from a microorganism belonging to the genus Pseudomonas which acts on L-sorbosone to produce 2-keto-L-gulonic acid.

Description: The novel coenzyme independent L-sorbosone dehydrogenase as defined below is an enzyme which catalyzes the oxidation of L-sorbosone to 2-keto-L-gulonic acid (hereinafter referred to as 2-KGA). 2-KGA is an important precursor for the production of Vitamin C. More exactly, the invention relates to the novel coenzyme independent L-sorbosone dehydrogenase which acts on L-sorbosone to produce 2-keto-L-gulonic acid originating from a microorganism belonging to the genus Pseudomonas and wherin the molecular structure consists of a single homogeneous subunit with a molecular weight of 47,000 ± 5,000 as measured by sodium dodecyl sulfate polyacrylamide gel electrophoresis. Reactions to convert L-sorbosone to 2-KGA using microorganisms are known. 2-KGA production from L-sorbosone using cell free extracts of microorganisms was reported in several prior publications. In U.S.P. No. 3,907,639, microorganisms belonging to the genus Acetobacter, Pseudomonas, Escherichia, Serratia, Bacillus, Staphylococcus, Aerobacter, Alcaligenes, Penicillium, Candida and Gluconobacter were reported to be capable of such a conversion. Furthermore, Kitamura et al., Europ. J. Appl. Microbiol., 2.1,(1975) reported that the L-sorbone oxidizing enzyme found in Gluconobacter melanogenes IFO3293 required neither coenzyme nor an electron acceptor for the development of enzyme activity. Makover et al., Biotechnol. Bioeng. 17,1485,(1975) reported the presence of L-sorbosone dehydrogenase activity in the particulate fraction of Pseudomonas putida ATCC 21812, but it has not been reported that the L-sorbosone dehydrogenase was isolated from Pseudomonas putida in the form of a homogeneous protein. Therefore, the physico-chemical properties of the enzyme have not been specified yet. The present invention relates to such novel enzyme having coenzyme independent L-sorbosone dehydrogenase activity and a process for producing this enzyme. It has been found that the purified enzyme isolated from a membrane fraction of cells of specific microorganisms catalyzes the oxidation of L-sorbosone to 2-KGA. The present invention has been accomplished on the basis of this finding. It is an object of the present invention to provide the novel enzyme having coenzyme independent L-sorbosone dehydrogenase activity to convert L-sorbosone to 2-KGA. It is another object to provide a process for producing this novel L-sorbosone dehydrogenase by cultivation of a microorganism belonging to the genus Pseudomonas or a mutant thereof which are capable of producing the novel L-sorbosone dehydrogenase in the cells, and isolating said enzyme in pure form from said cells. This isolation can be accomplished by disruption of the cells, and isolation and purification of the enzyme from the cell free extract of disrupted cells, preferably from the membrane fraction of microorganisms. The physico-chemical properties of the purified sample of the novel coenzyme independent L-sorbosone dehydrogenase prepared by Examples set forth later on are as follows: 1) Enzyme activity L-Sorbosone dehydrogenase, i.e. the enzyme of the present invention catalyzes the oxidation of L-sorbosone to 2-KGA in the presence of an electron acceptor according to the following reaction formula: The enzyme does not utilize oxygen as an electron acceptor. However, any conventional compound which has the ability to act as an electron acceptor can be utilized in conjunction with the enzyme of this invention to oxidize L-sorbosone to 2-KGA. As an electron acceptor, 2,6-dichlorophenolindophenol (hereinafter referred to as DCIP), phenazine methosulphate, Wurster's blue, ferricyanide, coenzyme Q or cytochrome C, etc. can be used. Assay of enzyme activity Enzyme assay was carried out at 25°C by measuring the decrease of absorbance at 600nm of DCIP spectrophotometrically. One unit of enzyme activity was defined as the amount of enzyme which catalyzed the reduction of 1 µmole of DCIP per minute. The extinction coefficient of DCIP at pH 7.0 was taken as 9.45mM⁻¹ The basal reaction mixture was prepared by mixing 6ml of 0.1M potassium phosphate buffer (pH 7.0) containing 0.3% Triton X-100, 0.45ml of 2.5mM DCIP and 10.35ml of water. A cuvette with 1cm light path contained 0.4ml of basal reaction mixture, 20µl of 10mM phenazine methosulfate, 10µl of enzyme solution and 20µl of 110mM L-sorbosone solution. A reference cuvette contained all the reagents except enzyme solution, but 10µl of water was added instead. The reaction was started by the addition of the substrate. 2) Substrate specificity Substrate specificity of the enzyme was determined using the same enzyme assay method as described in the above 1) except that 20µl of each of the various substrate solutions (100mM) was used instead of L-sorbosone. The results of the measurement are shown in Table 1. It was revealed that the enzyme of the present invention acts on a variety of aldehyde compounds. Substrate specificity of coenzyme independent L-sorbosone dehydrogenase from P. putida ATCC 21812 Substrate Relative activity (%) L-Sorbosone 100.0 Methylglyoxal 288.9 Glyoxal 172.2 Glutaraldehyde 147.2 Glyceraldehyde 88.9 Glycolaldehyde 83.3 Propionaldehyde 61.1 Glyoxilic acid 52.8 Benzaldehyde 27.8 Acetaldehyde 22.2 L-Idose 19.4 D-Mannose 0 D-Fructose 0 D-Glucose 0 L-Sorbose 0 3) Optimum pH The correlation between the reaction rate of the L-sorbosone dehydrogenase and pH was determined in potassium phosphate and Tris-HCl buffers. The result is shown in Table 2. The enzyme showed the highest enzyme activity at pH range between about 7.0 and about 8.0. Optimmum pH of coenzyme independent L-sorbosone dehydrogenase of P. putida ATCC 21812 pH Buffer (0.1 M) Relative activity (%) 6.0 Potassium phosphate 44.4 6.5 " 77.8 7.0 " 100.0 7.5 " 114.0 8.0 " 100.0 8.0 Tris-HCl 100.0 8.5 " 80.6 4) pH stability The purified enzyme was added to the buffers of various pH's for 24 hours at 4°C. The residual activity was assayed under the standard assay conditions as described in the above 1). The results of the measurement are shown in Table 3. The purified enzyme was relatively stable in alkaline pH and became unstable with the increase of acidity. pH stability of coenzyme independent L-sorbosone dehydrogenase of P. putida ATCC 21812 pH Buffer Relative activity (%) 4.0 Acetate 36.8 4.5 " 36.8 5.0 " 57.9 5.5 " 81.6 6.0 " 78.9 6.0 Potassium phosphate 68.4 6.5 " 73.7 7.0 " 100.0 7.5 " 94.7 8.0 " 105.3 8.0 Tris-HCl 89.5 8.5 " 94.7 5) Heat stability The purified enzyme was treated for 10 minutes at various temperatures in 10mM potassium phosphate buffer (pH 7.0), and then immediately cooled in iced water. The residual activity was measured under the standard assay conditions as described under 1) above. The results are shown in Table 4. This enzyme was unstable and lost about one half of its activity by the treatment at 30°C for 10 minutes. Thermostability of coenzyme independent L-sorbosone dehydrogenase of P. putida ATCC 21812 Temperature (°C) Relative activity (%) 4 100.0 20 82.9 30 54.3 40 40.0 50 11.4 60 8.6 6) Optimum temperature The enzymatic activities of L-sorbosone dehydrogenase were measured at temperatures from 10°C to 40°C in the reaction system as described under 1) above. The results are shown in Table 5. This enzyme showed its optimum temperature between about 20°C and about 40°C. Optimum temperature of coenzyme independent L-sorbosone dehydrogenase from P. putida ATCC 21812 Temperature (°C) Relative activity (%) 10 58.8 15 76.5 20 103.0 25 100 30 100 35 111.8 40 105.9 7) Molecular weight The purified enzyme with specific activity of 51.5 unit/mg protein was treated by sodium dodecyl sulfate (SDS) and was analyzed for its molecular weight of the subunit by SDS-polyacrylamide gel electrophoresis. It was proved that the enzyme consists of a single homogeneous subunit with a molecular weight of 47,000 ± 5,000. 8) Measurement of the Km value In the procedure described under 1) above, the velocities of oxidizing reactions with varying concentrations of L-sorbosone were measured to determine the apparent Michaelis constant (Km) for L-sorbosone. Km value was calculated to be 13 ± 2mM with DCIP and phenazine methosulfate as electron acceptors. 9) Effect of metal ions Using the assay procedure described under 1) above, the effect of various metal ions on the enzyme activity was examined. The results of the measurement are shown in Table 6. Cu²⁺ and Mn²⁺ strongly inhibited the enzyme. Effect of metal ions on coenzyme independent L-sorbosone dehydrogenase of P. putida ATCC 21812 Metal ion Concentration (mM) Relative activity (%) None 0 100.0 Cu²⁺ 0.8 0 Mn²⁺ 0.8 0 Ni²⁺ 4.0 48.9 Zn²⁺ 2.0 48.9 Co²⁺ 0.8 57.8 Fe³⁺ 0.8 68.9 Mo⁶⁺ 0.8 77.8 Mg²⁺ 4.0 100.0 10) Effect of inhibitors Using the assay procedure described under 1) above, the effect of inhibitors on the enzyme activity was examined. The results are shown in Table 7. Sodium azide and monoiodoacetate slightly inhibited the enzyme activity. Effect of inhibitors on coenzyme independent L-sorbosone dehydrogenase of P. putida ATCC 21812 Inhibitors Concentration (mM) Relative activity (%) None 0 100.0 NaN₃ 25.0 77.3 ICH₂COOH 5.0 88.6 11) Prosthetic group The absorption spectrum of the purified enzyme showed a peak at about 350nm and a wide shoulder at 380-420nm in the visible region. These absorption maxima were the characteristic of quinoprotein enzyme which had pyrroloquinoline quinone (hereinafter referred to as PQQ) as a prosthetic group. 12) Effect of addition of PQQ on the enzyme activity Using the assay procedure described under 1) above, the effect of addition of PQQ on the enzyme activity was examined. The results are shown in Table 8. Significant increase of the enzyme activity was observed by the addition of PQQ. Effect of PQQ on the activity of coenzyme independent L-sorbosone dehydrogenase of P. putida ATCC 21812 PQQ concentration (µM) Relative enzyme activity (%) 0 100 0.1 106 0.2 142 0.5 150 0.9 158 6.0 174 15.0 192 13) Purification method Purification of coenzyme independent L-sorbosone dehydrogenase may be effected by known purification methods and by a combination of known purification methods respectively, such as ion exchange chromatography, absorption chromatography, gel-filtration, gel-electrophoresis, salting out and dialysis. The coenzyme independent L-sorbosone dehydrogenase provided by the present invention can be prepared by cultivating an appropriate microorganism, disrupting the cells and isolating and purifying it from cell free extract of disrupted cells, preferably from the membrane fraction of microorganism. The microorganisms used for the present invention are microorganisms belonging to genus Pseudomonas or mutants thereof, preferably Pseudomonas putida. Microorganisms belonging to the genus Pseudomonas which are used in the present inventions can be isolated from natural sources or available from the culture collections. The mutants derived thereof may also be used according to the present invention. The mutants used in the present invention can be obtained by treating a wild type strain with a mutagen such as ultraviolet irradiation, X-ray irradiation, γ-ray irradiation or through contact with a nitrous acid or other suitable mutagens, or by isolating a clone occurring by spontaneous mutation. These mutations of a wild type strain or a mutant strain thereof may be effected in any of the ways well know per se for the particular purpose by one skilled in the art. Many of these methods have been described in various publications, for example, "Chemical Mutagens" edited by Y. Tajima, T. Yoshida and T. Kada, published by Kodansha Scientific Inc., Tokyo, Japan, in 1973. Examples of the strains most preferably used in the present invention are Pseudomonas putida ATCC 21812 and the like. Pseudomonas putida ATCC 21812 is available from American Type Culture Collection (12301 Parklawn Drive, Rockville, Maryland 20852, U.S.A.). The microorganism may be cultured in an aqueous medium supplemented with appropriate nutrients under aerobic condition. The cultivation may be conducted at pH of 4.0 to about 8.0, preferably from 5.5 to 7.5. A cultivation period varies depending upon the nutrient medium, preferably about 10 to 100 hours. A preferred temperature range for carrying out for the cultivation is from about 10°C to 40°C, preferably from 25°C to 35°C. It is usually required that the culture medium contains nutrients, e.g. assimilable carbon sources such as glycerol, D-mannitol, D-sorbitol, erythritol, ribitol, xylitol, arabitol, inositol, dulcitol, D-ribose, D-fructose, D-frucose, D-glucose, gluconate, maltose and sucrose, preferably D-sorbitol or glycerol; digestible nitrogen sources such as organic substances, for example, peptone, yeast extract, soybean meal and corn steep liquor and inorganic substances, for example, ammonium sulfate, ammonium chloride and potassium nitrite; vitamins and trace elements. In the following, an embodiment for isolation and purification of L-sorbosone dehydrogenase from the microorganisms after the cultivation is briefly described. (1) Cells are harvested from the fermentation broth by centrifugation. (2) The cells are suspended in the buffer solution and disrupted by means of a homogenizer, sonicator or treatment with lysozyme and the like to give a disrupted solution of cells. (3) L-sorbosone dehydrogenase is isolated and purified from cell free extract of disrupted cells, preferably from the membrane fraction of microorganisms. The L-sorbosone dehydrogenase provided by the present invention is useful as a catalyst for the production of 2-KGA from L-sorbosone. The reaction should be conducted at pH values of from about 5.0 to about 10.0 in the presence of an electron acceptor, for example, DCIP, phenazine methosulfate, Wurster's blue, ferricyanide, coenzyme Q, cytochrome C and the like in a solvent such as phosphate buffer, tris-HCl buffer and the like. A preferred temperature range for carrying out the reaction is from about 10°C to about 50°C. When the pH and temperature are set at about 7.0-8.0 and 30°C, respectively, reaction usually brings about most preferable results. Concentration of L-sorbosone in a solvent varies depending on other reaction conditions but, in general, is desirable to be about 10-100g/L, most preferably from about 30-40g/L. In the reaction, the enzyme may also be used in an immobilized state with an appropriate carrier. Any means of immobilizing enzyme generally known to the art may be used. For instance, the enzyme may be bound directly to a membrane, granules or the like of a resin having functional group(s), or it may be bound through bridging compounds having bifunctional group(s), for example, glutaraldehyde, to the resin. The following examples illustrate the present invention: Example 1. Preparation of L-sorbosone dehydrogenase 1) Cultivation of P. putida ATCC 21812 The agar slant culture of P. putida was inoculated into 5ml of the medium composed of 70g/L of glycerol, 15g/L of yeast extract (Oriental Co., Ltd.) and 2.5g/L of MgSO₄.7H₂O in a test tube, and incubated at 30°C for 2 days on a tube shaker (280 r.p.m.). Two ml of this culture was transferred to 100ml of the same medium in a 500ml-Erlenmeyer flask, and cultivated at 30°C for 20 hours on a rotary shaker (180 r.p.m.). The culture (400ml) thus prepared was used as an inoculum for a 30L-jar fermentor containing 20L of the same medium. The jar fermentor was operated at 30°C, 250 r.p.m. for agitation and 20L/min. for aeration. After 40 hours fermentation, the culture was harvested to collect the cells by centrifugation (8,000 r.p.m.,10,000g). From 20L of broth, 920g (wet weight) of the cells was obtained. The cells were frozen at -20°C until use. 2) Preparation of membrane fraction The frozen cells of P. putida (760g, wet weight) were thawed and suspended in 3,800ml of 0.85% NaCl solution. The cell suspension was then homogenized by a Dyno Mill homogenizer (Willy A. Bachofen Co., Basle) in the presence of glass beads (0.1mm in diameter) at 2,000 r.p.m. for 4 minutes at 4°C. The homogenate thus prepared was centrifuged at 1,800 x g for 10 minutes to remove the cell debris and glass beads. The resulting supernatant was centrifuged at 80,000 x g for 60 minutes, and then the precipitate was collected as membrane fraction (266g). 3) Solubilization of L-sorbosone dehydrogenase from membrane fraction The membrane fraction (266g, wet weight) was suspended in 1,100ml of 50mM potassium phosphate buffer, pH 7.0, containing 1% Triton X-100, stirred for 15 hours and centrifuged at 80,000 x g for 1 hour to obtain the supernatant. The supernatant (1,000ml) thus obtained was dialyzed against 20L of 10mM potassium phosphate buffer, pH 7.0, containing 0.1% Triton X-100 for 15 hours and used for DEAE-Sepharose CL-6B (Pharmacia Fine Chemicals) column chromatography. 4) DEAE-Sepharose CL-6B column chromatography (I) The dialyzed supernatant was applied to a DEAE-Sepharose CL-6B column (3.8⊘ x 30cm), which had been equilibrated with the same buffer described under 3) above. The column was washed with the same buffer, and the enzyme was eluted by a linear gradient of NaCl to 0.5M. 5) DEAE-Sepharose CL-6B column chromatography (II) The active fractions from the previous step were combined and dialyzed against the same buffer described under 3) above for 15 hours, and then applied to a DEAE-sepharose (diethylaminoethyl-agarose) CL-6B column (2.5⊘ x 25cm) equilibrated with the same buffer. The column was washed with the same buffer, and the enzyme was eluted by a linear gradient of NaCl to 0.3M. 6) DEAE(diethylaminoethyl-polyvinyl-type)-Toyopearl 650s (Toyo Soda) column chromatography The active fractions from the previous step were combined and dialyzed against the same buffer described under 3) above for 15 hours, and then applied to a DEAE-Toyopearl 650s column (2.0⊘ x 20cm) equilibrated with the same buffer. The column was washed with the same buffer, and then the enzyme was eluted by a linear gradient of NaCl to 0.1M. 7) Hydroxyapatite HCA 100S (Mitsui Toatsu) column chromatography The active fractions from the previous step were combined and dialyzed against 1mM potassium phosphate buffer (pH 7.0) containing 0.1% Triton X-100 for 15 hours, and then applied to a hydroxyapatite HCA 100S column (2.0⊘ x 10cm) equilibrated with the same buffer. The enzyme was eluted with the same buffer. 8) TSK-GEL(polyvinyl tpe) Toyopearl HW 60S (Toyo Soda) column chromatography I and II The active fractions from the previous step were combined and concentrated by ultrafiltration using the membrane filter (Diaflo PM-30, Amicon; polysulfone type; fractionation size: MG ∼30000) to a small volume (ca. 2ml). Then, the concentrate was applied to the column packed with TSK-GEL Toyopearl HW 60S (l.5cm⊘ x 80cm) in 10mM potassium phosphate buffer, pH 7.0, containing 0.1% Triton X-100. The column was developed by the same buffer. The active fractions were combined, concentrated and re-chromatographed on the same column. Summary of the purification procedure of L-sorbosone dehydrogenase is shown in Table 9. 9) Electrophoretic analysis The purified enzyme with specific activity of 51.5 unit/mg protein was treated by sodium dodecyl sulfate (SDS) and was analyzed for its purity by SDS-polyacrylamide electrophoresis. It was proved that the enzyme consists of a single homogeneous subunit with a molecular weight of 47,000 ± 5000. 10) Identification of the reaction product The reaction mixture containing 0.4ml of the purified enzyme solution, 0.05ml of 0.5M potassium phosphate buffer (pH 7.0), 0.05ml of 0.5M L-sorbosone and 0.02ml of 0.2M phenazine methosulfate was incubated at 30°C for 60 minutes. The reaction product was analyzed by thin layer chromatography and high performance liquid chromatography. As a result, the product was identified to be 2-keto-L-gulonic acid in comparison with an authentic sample. Example 2 The reaction mixture containing 5ml of purified coenzyme independent L-sorbosone dehydrogenase (total activity, 206 unit), as prepared by the manner as described in the steps (1) to (8) of the Example 1, 1ml of 0.5M potassium phosphate buffer (pH 7.0), 1ml of 1M L-sorbosone solution, 0.2ml of 0.2M phenazine methosulfate solution and 2.8ml of water were incubated at 25°C with gentle shaking. As a result, 2-KGA was formed with the rate of 350mg/hr.

Claims: The coenzyme independent L-sorbosone dehydrogenase which acts on L-sorbosone to produce 2-keto-L-gulonic acid originating from a microorganism belonging to the genus Pseudomonas and wherein the molecular structure consists of a single homogeneous subunit with a molecular weight of 47,000±5,000 as measured by sodium dodecyl sulfate polyacrylamide gel electrophoresis. The dehydrogenase according to claim 1, which has the following physico-chemical properties: a) prosthetic group: pyrroloquinoline quinone b) optimum pH: about 7 - about 8 c) optimum temperature: about 20°C - about 40°C d) thermostability: unstable at temperatures higher than ca. 30 °C e) inhibition: by Cu²⁺ and Mn²⁺ ions. A coenzyme independent L-sorbosone dehydrogenase according to claim 1, which is a membrame-bound enzyme of Pseudomonas putida ATCC 21812 or a mutant thereof which perfoms the same same function as the parent strain. A process for producing a novel coenzyme independent L-sorbosone dehydrogenase according to claim 1 which comprises cultivating, in a cultivation medium, a microorganism belonging to the genus Pseudomonas or a mutant thereof which are capable of producing the novel coenzyme independent L-sorbosone dehydrogenase in cells, disrupting the cells, isolating and purifying it from the cell free extract of the disrupted cells, from the membrane fraction of microorganism. A process according to the claim 4, wherein the microorganism is Pseudomonas putida ATCC 21812 or a mutant thereof which perfoms the same function as the parent strain. A process for producing 2-keto-L-gulonic acid comprising oxidizing L-sorbosone in the presence of a catalyst, said catalyst being the enzyme with L-sorbosone dehydrogenase activity of claim 1. The use of the enzyme of claim 1 in the microbial production of 2-ketogulonic acid.

Inventors: 1HOSHINO, TATSUO, FUJIWARA, AKIKO
Applicants: F. HOFFMANN-LA ROCHE AG
Application year: 1988
Main classification: C12N9
IPC codes: C12P7, C12N9, C12R1