Method for producing sodium hyaluronate by fermentation method

Abstract: A method of producing sodium hyaluronate by a fermentation method comprises culturing a mutant strain FM 300 derived from Streptococcus equi and partially free from auxotophy to thereby stably produce sodium hyaluronate and accumulating the hyaluronate.

Description: BACKGROUND OF THE INVENTION This invention relates to a method for producing sodium hyaluronate by a fermentation method and, in more detail, to a method for producing and accumulating sodium hyaluronate by culturing a mutant strain derived from Streptococcus equi ATCC 9527 and partially free from auxotrophy. Heretofore, sodium hyaluronate was extracted from rooster's comb, vitreous bodies of eyes of cattle or umbilical card. However, the method of extraction for preparation of sodium hyaluronate has the drawback of highly complicated isolation and purification. For overcoming this drawback, there is proposed in Japanese Unexamined Patent Publications Nos. 56692/1983 and 63294/1986 a method consisting in culturing a microorganism having the ability of producing sodium hyaluronate and directly collecting sodium hyaluronate from the culture liquid. However, this method has the drawback that the amount of production is unstable from lot to lot and it is difficult to practice the method industrially. Alternatively, there is proposed a method for stably producing sodium hyaluronate at high yield without variation, using a mutant strain FM 100 derived from Streptococcus equi (Japanese Unexamined Patent Publication No. 123392/88). Although the productivity of sodium hyaluronate at the initial stage by this method is highly enough, the yield gradually decreases in case of repeated culturing for a long period of time or a semi-continuous culturing in which a fresh culture medium is added to a culture liquid which has been partially left behind, leading to unstable production of sodium hyaluronate. On the other hand, a solution containing sodium hyaluronate obtained by a fermentation method contains high molecular compounds and metals as impurities, which need be separated and removed. To this end, various proposals have been made in the art, such as the method of adsorption by ion exchange resins, activated charcoal, diatomaceous earth or magnesium silicate, the method of treatment with quaternary ammonium salts or proteases, the method of extraction or precipitation by solvents such as ethanol, aceton, butanol or phenol, or the method of treatment with membrane filters. These methods, however, are complicated in purification and are unsatisfactory for preparing sodium hyaluronate of high purity. SUMMARY OF THE INVENTION It is a principal object of the present invention to provide a method for preparing sodium hyaluronate easily and at a high yield. It is another object of the present invention to provide a method for producing sodium hyaluronate which may be utilized for medicaments and by which sodium hyaluronate of high purity may be produced. It is yet another object of the present invention to provide a method for producing sodium hyaluronate which is highly stable in production. The above and other objects of the invention will become apparent from the following description. According to the present invention, there is provided a method for producing sodium hyaluronate by a fermentation method comprising preparing a mutant strain FM 300 derived from Streptococcus equi and being partialy free from auxotrophy, culturing said mutant strain to thereby stably produce sodium hyaluronate and accumulating the hyaluronate. PREFERRED EMBODIMENTS OF THE INVENTION In the present invention, the mutant strain FM 300, derived from Streptococcus equi and partially free from auxotrophy, is additionally free from auxotrophy with respect to a strain FM 100 derived from Streptococcus equi. The strain FM 300 has been deposited in the Fermentation Research Institute under the International Deposit No. BP-2319. There is no limitation to a culture medium or culturing conditions for producing the mutant strain FM 300 from its parent strain Streptococcus equi by mutation. For such mutation, for example, the mutant strain FM 100 of Streptococcus equi is firstly produced using Streptococcus equi ATCC 9527 as mentioned hereinbelow. The mutant strain FM 100, derived from steptococcus equi and partially free from auxotrophy, may be produced by mutation of the known strain Streptococcus equi ATCC 9527 as the parent strain. This mutant strain FM 100 has been deposited in Fermentation Research Institute under International Deposit No. BP-2396. There is no limitation to a culture medium or culturing conditions employed in mutating the parent strain Streptococcus equi to the strain FM 100, if the strain FM 100 may be produced from the parent strain Streptococcus equi. For such mutation, for example, Streptococcus equi ATCC 9527 is cultured in a culture medium containing 1.5 wt.% of polypeptone, 0.5 wt.% of yeast extract and 2 wt.% of glucose at 33°C, and the strain in the log phase is collected at a lower temperature by centrifuging and washed thrice in an asceptic condition using physiological saline. The resulting cells are shaken at 30°C for one hour in a 0.05 M phosphate buffer at pH of 5.0 containing 50 µg/ml of N-methyl-N′-nitro-N-nitrosoguanidine and cooled with ice. The resulting cells are washed thrice at a lower temperature using physiological saline, cultured at 33°C for three hours in a culture medium containing 1.5 wt.% of polypeptone, 0.5 wt.% of yeast extract and 2 wt.% of glucose, washed thrice at a lower temperature using physiological saline, and cultured at 33°C for seven days in a first chemically defined medium shown in Table 1. The culture liquid obtained after multiplication is inoculated in a new one of the first chemically defined culture medium shown in Table 1. After repeating the above operation thrice, the resulting culture liquid is spread on a first chemically defined medium of the same composition containing agar and the resulting colony is isolated. Components of First Chemically Defined Medium Concentration (mg/ℓ) Components of First Chemically Defined Medium Concentration (mg/ℓ) glucose 10000 D,L-calcium pantothenate 0.5 L-alanine 200 riboflavin 0.5 L-arginine 200 thiamine 0.5 L-asparagine 200 niacin 1.0 L-aspartic acid 200 pyridoxamine 1.0 L-cysteine 100 pyridoxal 1.0 L-glutamine 350 folic acid 0.005 L-glutamic acid 1000 biotin 0.0025 glycine 400 p-aminobenzoic acid 0.1 L-histidine 400 NAD ⊕ 0.5 L-hydroxyproline 50 K₂HPO₄ 500 L-isoleucine 200 KH₂PO₄ 14000 L-leucine 200 MgSO₄·7H₂O 200 L-lysine 200 FeSO₄·7H₂O 10 L-methionine 200 MnSO₄·4H₂O 10 L-phenylalanine 200 NaCℓ 10 L-proline 200 NaC₂H₃O₂·3H₂O 10000 L-serine 200 (sodium acetate) L-threonine 200 NaHCO₃ 500 L-tryptophane 200 CaCℓ₂·2H₂O 60 L-tyrosine 200 L-valine 200 adenine 20 guanine 20 uracil 20 Table 2 shows auxotrophy of the strain FM 100 derived from the parent strain Streptococcus equi. It is seen from this Table that the strain FM 100 differs from its parent strain Streptococcus equi in that it is partially free from auxotrophy among its bacteriological properties. Nutrient Demand Nutrient Demand Nutrient Demand L-alanine No L-methionine Yes D,L-calcium pantothenate Yes L-arginine Yes L-phenylalanine Yes riboflavin Yes L-aspartic acid No L-proline No thiamine Yes L-cysteine Yes L-serine No niacin No L-glutamine Yes L-threonine Yes pyridoxamine No L-glutamic acid No L-tyrosine Yes pyridoxal Yes glycine No L-tryptophane Yes folic Acid No L-histidine Yes L-valine Yes biotin Yes L-isoleucine Yes p-aminobenzoic acid No L-leucine Yes adenine Yes NAD ⊕ Yes L-lysine Yes uracil No The strain FM 100 derived by mutation from the Streptococcus equi, e.g. by the method described above, is then cultured in a culture medium containing 1.5 wt.% of polypeptone, 0.5 wt.% of yeast extract and 2 wt.% of glucose at 33°C, the strain in the log phase is collected at a lower temperature by centrifuging and washed thrice in an aseptic condition using physiological saline. The resulting cells are shaken at 30°C for one hour in a 0.05 M phosphate buffer at pH of 5.0 containing 50 µg/ml of N-methyl-N′-nitro-N-nitrosoguanidine and cooled with ice. The resulting cells are washed thrice at a lower temperature using physiological saline, cultured at 33°C for three hours in a culture medium containing 1.5 wt.% of polypeptone, 0.5 wt.% of yeast extract and 2 wt.% of glucose, washed thrice at a lower temperature using physiological saline, and cultured at 33°C for seven days in a second chemically defined medium shown in Table 3. The culture liquid obtained after multiplication is inoculated in a new one of the second chemically defined medium shown in Table 3. After repeating the above operation thrice, the resulting culture liquid is spread on a second chemically defined medium of the same composition containing agar and the resulting colony is isolated. Components of Second Chemically Defined Medium Concentration (mg/ℓ) Components of Second Chemically Defined Medium Concentration (mg/ℓ) glucose 10000 D,L-calcium pantothenate 0.5 L-arginine 200 riboflavin 0.5 L-cysteine 100 thiamine 0.5 L-glutamine 350 pyridoxal 1.0 L-histidine 400 biotin 0.0025 L-isoleucine 200 NAD ⊕ 0.5 L-leucine 200 K₂HPO₄ 500 L-lysine 200 KH₂PO₄ 14000 L-methionine 200 MgSO₄·7H₂ 200 L-tryptophane 200 FeSO₄·7H₂O 10 L-tyrosine 200 MnSO₄·4H₂O 10 L-valine 200 CaCℓ₂·2H₂O 60 adenine 20 Table 4 shows auxotrophy of the strain FM 300 derived from the parent strain Streptococcus equi. It is seen from this Table that the strain FM 300 differs from its parent strain Streptococcus equi ATCC 9527 in that it is partially free from auxotrophy among its bacteriological properties, while also differing from the strain FM 100 derived by mutation from Streptococcus equi in that it is additionally free from auxotrophy in connection with the demand for L-phenylalanine and L-threonine. Nutrient Demand Nutrient Demand Nutrient Demand L-alanine No L-methionine Yes D,L-calcium pantothenate Yes L-arginine Yes L-phenylalanine No riboflavin Yes L-aspartic acid No L-proline No thiamine Yes L-cysteine Yes L-serine No niacin No L-glutamine Yes L-threonine No pyridoxamine No L-glutamic acid No L-tyrosine Yes pyridoxal Yes glycine No L-tryptophane Yes folic acid No L-histidine Yes L-valine Yes biotin Yes L-isoleucine Yes p-aminobenzoic acid No L-leucine Yes adenine Yes NAD ⊕ Yes L-lysine Yes uracil No According to the present invention,the above described method for deriving the mutant strain FM 300 by mutation from their parent strain Streptococcus equi is merely illustrative and it suffices that the strains free from auxotrophy in the above described manner may be derived. The culture media employed for producing sodium hyaluronate using the strain thus rendered free of auxotrophy may be those customarily employed for producing microorganisms. For example, carbon sources such as glucose, fructose, galactose or sucrose, inorganic salts such as dipotassium hydrogenphosphate, potassium dihydrogenphosphate, magnesium sulfate, sodium sulfite or sodium thiosulfate, diammonium hydrogenphosphate, or organic nutrient sources, such as polypeptone, casamino acid, yeast extract, corn steep liquor or soybean hydrolysate liquid, may be employed. If necessary, various amino acids or vitamins may also be advantageously employed. These ingredients or components of the culture media may be charged collectively or divisionally, as desired. The culturing for producing sodium hyaluronate according to the present invention may be performed by any known method, such as culturing under aeration and agitation, and preferably at a culturing temperature of 30 to 35°C. Since the pH of the culture liquid is lowered with the growth of the bacteria, the pH adjustment agents, such as sodium hydroxide, potassium hydroxide or ammonia are preferably added to the liquid for adjusting the pH value within the range from 6.5 to 9.0. During such culturing, the culture liquid is gradually increased in viscosity with product of sodium hyaluronate. Therefore, the culturing is terminated at the time point when the carbon source employed as the culture medium is used up in the culture liquid. The culture broth thus obtained is then purified to give sodium hyaluronate. A portion of the culture liquid may be left after termination of culturing and a new culture medium may be added thereto by way of performing semi-continuous culturing. According to the present invention, for purifying a crude product for producing pure sodium hyaluronate after termination of culturing as mentioned hereinabove, preferably the cells are removed by centrifugation, filtration or with the aid of flocculants, carbon or celite, and then water and an organic solvent are added to the liquid to produce a cell free solution containing sodium hyaluronate, which is then subjected to a purifying process. If the solution containing sodium hyaluronate is prepared only with water without employing the organic solvent, problems are presented during the purifying process that pyrogens, proteins or metals cannot be removed sufficiently. Although any organic solvents miscible with water may be employed, such as alcohols, e.g. methanol, ethanol or propanol, or acetone, those of the grade of the reagents are preferably employed, in order that sodium hyaluronate may be used as the medicament. According to the present invention, purification may be performed by adding the aforementioned organic solvents to the solution containing sodium hyaluronate, or by dissolving sodium hyaluronate in an aqueous organic solvent of a predetermined concentration. The concentration of the organic solvent may be selected within a wide range as long as sodium hyaluronate is not precipitated. However, for most stable effects, the organic solvent is preferably contained in an amount of 20 to 50 wt.% in the solution containing sodium hyaluronate. It is also preferred that the solution containing sodium hyaluronate be diluted with water and the organic solvent so that the concentration of sodium hyaluronate in the solution is within the range from 0.1 to 5g/ℓ. According to the present invention, the purification may be performed by contacting the solution containing sodium hyaluronate with alumina, activated charcoal, or "FLORISIL" manufactured by Floridin Co., Ltd. and then contacting the solution with silica gel. The alumina is preferably aluminum oxide and produced in general by dehydrating and calcining aluminum hydroxide at elevated temperatures. However, this is not limitative of the present invention. Depending on the particle size, the alumina is classified into a fine size alumina (with the particle size of not more than 10 µm), a medium size alumina (with the particle size of 40 to 60 µm) and coarse size alumina (with the particle size of not less than 70 µm). Depending on the contents of alumina or impurities, there are various grades of alumina available on the market, such as so-called high purity alumina having the purity of about 99.99 %, besides the ordinary grade alumina with the purity of 90 to 99 %. There is also a so-called low soda alumina purified to have sodium oxide contents in the alumina of not higher than 0.1 %, in contrast to the ordinary sodium oxide contents in alumina of 0.3 to 0.4 %. There is also an activated alumina having a surface area of 50 to 400 m²/g and correspondingly high adsorption properties. Any of these types of alumina may be employed in the present invention. Also, any types of alumina may be employed in the present invention without regard to the mineral types such as α, β or γ or the particulate shape, such as honeycomb, granular or spherical shape. In treating the solution containing sodium hyaluronate with alumina, the pH value of the solution containing sodium hyaluronate is preferably 3 to 10 and more preferably 6 to 9, the temperature is preferably 0 to 40°C and the concentration of sodium hyaluronate is preferably 0.1 to 5 g/ℓ and more preferably 0.5 to 2 g/ℓ. For treating the solution with alumina, the method of adding pulverulent or particulate alumina to the solution containing sodium hyaluronate and stirring the mixture in a batch-wise system, or the method of charging particulate or molded alumina into a packing column and passing the solution through the packed column, may be employed. Although these methods may be combined or performed repeatedly, it usually suffices to perform the treatment only once, depending on the selection of the treating conditions. For contacting the solution containing sodium hyaluronate with the alumina, the packed column system is more effective than the batch type system. For treating the solution containing sodium hyaluronate by a column packed with alumina, the packed height of the column or the linear velocity of the solution may be suitably selected by taking the particle size of the alumina into account. Thus, the processing speed by the packed column system is preferably SV = 0.1 to 2, in consideration of the column clogging and the processing efficiency. Although pyrogens, proteins or nucleic acids may be removed by the treatment with alumina, metallic impurities, such as magnesium, calcium, silicon, iron or aluminum cannot be removed sufficiently. Therefore, according to the present invention, the solution treated with alumina need be contacted with silica gel. When the solution containing sodium hyaluronate is contacted with silica gel, the pH of the solution is preferably 3 to 12, the temperature is preferably 0 to 40°C and the concentration of sodium hyaluronate in the solution is preferably 0.1 to 5g/ℓ and more preferably 0.5 to 2g/ℓ. The pH value of less than 3 is not desirable since sodium hyaluronate is decomposed and the viscosity is increased to lower the operability. The pH value in excess of 12 is also not preferred since sodium hyaluronate tends to be decomposed. The temperature higher than 40°C is also not desirable since sodium hyaluronate tends to be decomposed so that the molecular weight is lowered. The concentration of sodium hyaluronate less than 0.1 g/ℓ is also not desired since the processing efficiency tends to be decreased and the concentration of sodium hyaluronate more than 5 g/ℓ is also not desired since the viscosity is increased to render the operation more difficult. According to the present invention, the silica gel is produced by decomposing sodium silicate with an inorganic acid, coagulating and washing the resulting product with water for removing impurities and drying the resulting product. However, the present invention is not limited to this method. For example, the commercially available silica gel of various grades used for dehumidification or drying in general, drying of gas or air, dehydration of organic solvents or for purification in general and having different values of particle size, pore diameter, shape, surface area or pH of the slurry, may also be employed. The particle size of 30 to 200 µm of the silica gel is preferred. If the particle size is less than 30 µm, the operability in removing the silica gel is lowered, while the column tends to be stopped when charged with the silica gel for chromatography. On the other hand, if the particle size is above 200 µm, the efficiency of removal of the metallic impurities is lowered. The silica gel preferably has the lower contents and amounts of eluation of the metallic impurities. For treating the alumina-treated solution containing sodium hyaluronate, the silica gel is packed in a packing column. The packed height of the column and the linear velocity of the solution containing sodium hyaluronate are preferably selected as a function of the particle size of the silica gel or the concentration of sodium hyaluronate. Thus, the processing speed SV is preferably 0.1 to 3. The relative amount of the silica gel to the solution containing sodium hyaluronate need be selected as a function of the contents of the metallic impurities in the sodium hyaluronate containing solution. Usually, the silica gel is used in an amount of 10 to 300 parts by weight for purifying 1 part by weight of sodium hyaluronate. In the method of the present invention, since sodium hyaluronate is produced by the fermentation method using a specific strain, sodium hyaluronate may be produced easily and at a high yield and stable output. Also the high purity sodium hyaluronate utilizable for medicaments may be produced by the purification process employing alumina and silica gel. EXAMPLES OF THE INVENTION The present invention will be explained hereinbelow in more detail with reference to Examples and Comparative Examples. However, these Examples are given for illustration only and are not intended for limiting the scope of the invention. In the following Examples and Comparative Examples, the percentage (%) denotes weight %. Example 1 To 1 lit. of a culture medium, pH 8.5, containing 2 % of glucose, 0.2 % of dipotassium hydrogenphosphate, 0.05 % of magnesium sulfate heptahydrate, 0.1 % of sodium thiosulfate, 1.0 % of polypeptone and 0.5 % of yeast extract was inoculated 10 ml of a pre-culture liquid of the mutant strain FM 300 of Streptococcus equi consisting of the same culture medium, and culturing was performed at the aeration of 1.5 volume volume minute (vvm), an agitating speed of 200 rpm and at the temperaturte of 33°C, as the pH was adjusted to 8.5 using sodium hydroxide. 2 % of glucose was added after 15 hours and 900 ml of a culture liquid was extracted at the time point when the total amount of glucose was consumed. There was further added 900 ml of a medium, pH 8.5, containing 2 % of glucose, 0.2 % of dipotassium hydrogenphosphate, 0.05 % of magnesium sulfate heptahydrate. 0.1 % of sodium thiosulfate, 1.0 % of polypeptone and 0.5 % of yeast extract, and culturing was performed at the aeration of 1.5 volume volume minute (vvm), an agitating speed of 200 rpm and at the temperature of 33°C, as the pH was adjusted to 8.5 using sodium hydroxide. 2 % of glucose was added after 5 hours and 900 ml of a culture liquid was extracted at the time point when the total amount of glucose was consumed. Table 5 shows the yield of sodium hyaluronate when the above described semi-continuous operation was repeated five times so that the total of six batch-wise operations were performed. The produced culture broth was adjusted to a pH value of 4 with hydrochloric acid, diluted by two times of volume with distilled water and freed of cells by centrifugation. The produced liquid was neutralized with sodium hydroxide and admixed with ethyl alcohol to precipitate sodium hyaluronate. After filtration, sodium hyaluronate was dissolved in water and admixed with cetyl pyridinium chloride and the produced precipitate was recovered by filtration and again dissolved in 2% saline. The resulting product was again repeatedly precipitated in ethyl alcohol. The produced sodium hyaluronate was dried in vacuum at room temperature to produce white colored sodium hyaluronate. Then, measurement of the nuclear magnetic resonance, infrared absorption spectrum and elementary analysis was performed to identify the product to be sodium hyaluronate. The following show the results of measurements. Elementary Analysis C H N Na Calcd. (%) 41.90 5.02 3.49 5.73 Found (%) 41.65 5.11 3.47 5.94 IR; 3400 cm⁻¹ (OH, NH), 2900 cm⁻¹ (CH), 1600 cm⁻¹ (C = O, COO⁻), 1560cm⁻¹(NH), 1400 cm⁻¹, 1040 cm⁻¹ ¹H-NMR (D₂O) 2.0 ppm (3H), 2.6 to 4.1 (10H), 4.2 to 5.0 (2H) Number of Batches Yield of sodium hyaluronate in g (per 1 lit. of cultured liquid) 1 7.3 2 6.8 3 6.9 4 6.9 5 6.5 6 6.7 Example 2 15 ℓ of a culture broth cultured by using a mutant strain FM 300 derived from Streptococcus equi was diluted to 50 ℓ with pure water so that the concentration of sodium hyaluronate was 1.10 g/ℓ. The centrifugation and the hollow fiber type ultrafiltration were then carried out to remove the cells and the components of the culture medium. 150 g of table salt was dissolved in 5000 ml of the solution containing sodium hyaluronate to adjust the pH to 7. The solution was then precipitated with 500 ml of ethanol, washed in 1000 ml of ethanol and dried in vacuum at 40°C to produce 4.9 g of sodium hyaluronate. 1.0 g of the semi-purified sodium hyaluronate product was dissolved in 700 ml of water and admixed with 300 ml of ethanol to produce a mixed solution of 0.1 % sodium hyaluronate. 500 ml of the mixed solution was passed through a glass column with the inside diameter of 5 cm and the height of 30 cm, packed with 150 g of 300 mesh size activated alumina for chromatography produced by Wako Pure Chemical Industries Ltd. and thoroughly washed with pure water, at a rate of SV = 0.4 (60 ml/h). The mixed solution thus treated with alumina was then passed through a second column of the same type as above packed with 150 g of silica gel manufactured by Wako Pure Chemical Industries Ltd. under the trade name of "WAKO GEL Q-50", at a rate of SV = 0.7 (105 ml/h). 500 ml of the liquid passed through the second column was collected, admixed with 15 g of table salt, adjusted to pH of 7, precipitated with 750 ml of ethanol, washed with 100 ml of ethanol and dried in vacuum at 40°C to produce 0.48 g of sodium hyaluronate. The following analyses were conducted on the thus produced sodium hyaluronate. Table 6 shows the results of these analyses. 1) Protein Contents: The protein contents were measured by the Lowry's method, with the purified sodium hyaluronate dissolved in 0.1 N sodium hydroxide. 2) Pyrogen Contents: The exothermic materials were measured by colorimetric analyses using a Toxicolor System produced by Seikagaku Kogyo Co., Ltd. 3) Metals: The metals were measured by a photographic dry plate system using an emission spectroanalytic system manufactured by Nippon Jarrell-Ash Co., Ltd. Comparative Example 1 Sodium hyaluronate was purified and analyzed by the same method as that shown in Example 2, except using water in place of ethanol, with the exception of ethanol used for precipitation. The results are shown in Table 6. Analyzed Item E.x 2 Comp. Ex. 1 Protein Contents 0.003 % 0.08 % Pyrogen Contents 5 pg/mg 97 pg/mg Metals aluminum Not More Than 10 ppm 100 to 1000 ppm silicon Not More Than 10 ppm 100 ppm iron Not More Than 10 ppm 10 to 100 ppm magnesium Nearly Zero 10 ppm Example 3 To 1 lit. of a culture medium, pH 8.5, containing 2 % of glucose, 0.2 % of dipotassium hydrogenphosphate, 0.05 % of magnesium sulfate heptahydrate, 0.1 % of sodium thiosulfate, 1.0 % of polypeptone and 0.5 % of yeast extract was inoculated 10 ml of a pre-culture liquid of the mutant strain FM 300 of Streptococcus equi consisting of the same culture medium, and culturing was performed at the aeration of 1.5 volume volume minute (vvm), an agitating speed of 200 rpm and at the temperaturte of 33°C, as the pH value was adjusted to 8.5 using sodium hydroxide. 2 % of glucose was added after 15 hours and 900 ml of a culture liquid was extracted at the time point when the total amount of glucose was consumed. The produced culture broth was adjusted to a pH value of 4 with hydrochloric acid, diluted by two times of volume with distilled water and freed of cells by centrifugation. The produced liquid was neutralized with sodium hydroxide and admixed with ethyl alcohol to precipitate sodium hyaluronate. After filtration, sodium hyaluronate was dissolved in water and admixed with cetyl pyridinium chloride and the produced precipitate was recovered by filtration and again dissolved in 2 % saline. The resulting product was again repeatedly precipitated in ethyl alcohol. The produced sodium hyaluronate was dried in vacuum at room temperature to produce 7.7 g of white colored sodium hyaluronate per liter of culture liquid. Then, measurement of the nuclear magnetic resonance, infrared absorption spectrum and elementary analysis was performed to identify the product to be sodium hyaluronate. The similar results to Example 1 were obtained to reveal that the product obtained was sodium hyaluronate. The same culturing operations were repeated 14 times, thus totalling 15 baches. The results are shown in Table 7. Number of Batches Yield of sodium hyaluronate in g (per 1 lit. of cultured liquid) 1 7.1 4 7.3 8 7.0 12 7.1 15 7.2 After prolonged culturing, the yield of sodium hyaluronate remained perpetually stable. Comparative Example 2 To 1 lit. of a culture medium, pH 8.5, containing 2 % of glucose, 0.2 % of dipotassium hydrogenphosphate, 0.05 % of magnesium sulfate heptahydrate, 0.1 % of sodium thiosulfate, 1.0 % of polypeptone and 0.5 % of yeast extract was inoculated 10 ml of a pre-culture liquid of the mutant strain FM 100 derived from Streptococcus equi consisting of the same culture medium as above, and culturing was performed at the aeration of 1.5 volume volume minute (vvm), an agitating speed of 200 rpm and at the temperature of 33°C, as the pH value was adjusted to 8.5 using sodium hydroxide. 2 % of glucose was added after 15 hours and the culturing was terminated at the time point when the total amount of glucose was consumed. The culture broth was adjusted to a pH value of 4 with hydrochloric acid, diluted by two times of volume with distilled water and freed of the cells by centrifugation. The produced cell free liquid was admixed with ethyl alcohol to precipitate sodium hyaluronate. After filtration, sodium hyaluronate was dissolved in water and admixed with cetyl pyridinium chloride and the produced precipitate was recovered by filtration and again dissolved in 2% saline. The resulting product was repeatedly precipitated in ethyl alcohol. The produced sodium hyaluronate was dried in vacuum at room temperature to produce 7.0 g of white colored sodium hyaluronate per lit. of the culture liquid. Similarly to Example 3, the same culturing operations were repeated 15 times in total. Sodium hyaluronate obtained was 7.0 g at the first batch, 7.3 g at the 4th batch, 3.9 g at the 8th batch, 6.3 g at the 12th batch and 4.3 g at the 15 batch, respectively. The yield was low as compared with Example 3 and was widely varied.

Claims: A method for producing sodium hyaluronate by a fermentation method comprising preparing a mutant strain FM 300 (FRI BP-2319) derived from Streptococcus equi and being partially free from auxotrophy, culturing said mutant strain to thereby stably produce sodium hyaluronate and accumulating said hyaluronate. The method according to claim 1 wherein the mutant strain FM 300 (FRI BP-2319) derived from said Streptococcus equi is produced by mutation from the mutant strain FM 100 (FRI BP 2396) derived from said Streptococcus equi. The method according to any of claims 1 and 2, wherein the mutant strain FM 300 (FRI BP-2319) derived from said Streptococcus equi is produced by chemical mutation, preferably in the presense of N-methyl-N'-nitro-N-nitrosoguanidine. The method according to any of claims 1 to 3 wherein the auxotrophy of the mutant strain FM 300 (FRI BP 2319) of Streptococcus equi is as shown in the following Table: Nutrient Demand Nutrient Demand Nutrient Demand L-alanine No L-methionine Yes D,L-calcium pantothenate Yes L-arginine Yes L-phenylalanine No riboflavin Yes L-aspartic acid No L-proline No thiamine Yes L-cysteine Yes L-serine No niacin No L-glutamine Yes L-threonine No pyridoxamine No L-glutamic acid No L-tyrosine Yes pyridoxal Yes glycine No L-tryptophane Yes folic Acid No L-histidine Yes L-valine Yes biotin Yes L-isoleucine Yes p-aminobenzoic acid No L-leucine Yes adenine Yes NAD ⊕ Yes L-lysine Yes uracil No The method according to any of claims 2 to 4, wherein the mutant strain FM 100 (FRI BP-2396) derived from Streptococcus equi ATCC 9527 is mutated preferably in the presence of N-methyl-N'-nitro-N-nitrosoguanidine to obtain the mutant strain FM 300 (FRI BP-2319). The method according to any of claims 2 to 5 wherein to prepare the mutant strain FM 300 (FRI BP-2319), the mutant strain FM 100 (FRI BP-2396) derived from said Streptococcus equi is cultured in a second chemically defined medium containing glucose, L-arginine, L-cysteine, L-glutamine, L-histidine, L-isoleucine, L-leucine, L-lysine, L-methionine, L-tryptophane, L-tyrosine, L-valine, adenine, D,L-calcium pantothenate, riboflavin, thiamine, pyridoxal, biotin, NAD ⊕ , K₂HPO₄, KH₂PO₄, MgSO₄·7H₂O, FeSO₄·7H₂O, MnSO₄·4H₂O and CaCl₂·2H₂O. The method according to any of claims 1 to 6 wherein a culture medium for culturing the mutant strain FM 300 (FRI BP-2319) derived from said Streptococcus equi to produce sodium hyaluronate is employed, the components of which are selected from the group consisting of carbon sources, inorganic salts, organic nutrient sources, amino acids, vitamins and mixtures thereof. The method according to any of claims 1 to 7 wherein a portion of a culture liquid is left after termination of said culturing and a new culture medium is added thereto to perform culturing semi-continuously. The method according to any of claims 1 to 7 wherein the culturing is discontinued at a time point when the carbon source is consumed. The method according to any of claims 1 to 9 wherein the sodium hyaluronate is purified after being freed of the mutant strain. The method according to claim 10 wherein the sodium hyaluronate freed of the mutant strain is admixed with water and an organic solvent to produce a solution containing sodium hyaluronate and the solution is then purified. The method according to claim 11 wherein the purification is performed by contacting said solution containing sodium hyaluronate with a substance selected from the group consisting of alumina, activated charcoal, and mixtures thereof and subsequently with silica gel.

Inventors: CHIBA SUSUMU C O DENKI KAGAKU, HASHIMOTO MASAMICHI C O DENKI, KITAGAWA HIRONOSHIN C O DENKI, MIYOSHI TERUZO C O DENKI KAGAK, SAEGUSA HARUHISA C O DENKI KAG, CHIBA, SUSUMU C/O DENKI KAGAKU KOGYO K.K., HASHIMOTO, MASAMICHI C/O DENKI KAGAKU KOGYO K.K., KITAGAWA, HIRONOSHIN C/O DENKI KAGAKU KOGYO K.K., MIYOSHI, TERUZO C/O DENKI KAGAKU KOGYO K.K., SAEGUSA, HARUHISA C/O DENKI KAGAKU KOGYO K.K.
Applicants: DENKI KAGAKU KOGYO KK, DENKI KAGAKU KOGYO KABUSHIKI KAISHA
Application year: 1989
Main classification: C12P19
IPC codes: C12P19