Process for production of biotin

Abstract: There is disclosed a process for the production of biotin, in which a culture of a microorganism of the genus Sphingomonas , having an ability to produce biotin, is prepared in a medium, and biotin produced and accumulated in the medium is collected. Also disclosed are microorganisms of the genus Sphingomonas , having an ability to produce biotin, which are useful for this production process of the present invention.

Description: The present invention relates to a process for the production of biotin and microorganisms for use in this process. Biotin is one of the vitamins required for human beings, animals, vegetables and certain kinds of microorganisms. As a process for the production of biotin using a microorganism, there have heretofore been known various processes using a microorganism such as those of the genus Streptomyces or Micromonospore (JP-B 41-21756); Sporobolomyces (JP-B 42-3074); Bacillus (JP-A 56-160998); Escherichia (JP-A 61-149091); Serratia (JP-A 2-27980); and Brevibacterium (JP-A 3-240489). These conventional processes are, however, not always satisfactory because of their low yield of biotin produced by any such microorganism. It is, therefore, required to develop a process for the production of biotin using a microorganism with higher efficiency, which is suitable for the biotin production on an industrial scale. Under these circumstances, the present inventors have intensively sought microorganisms having an increased ability to produce biotin over the nature and various type culture collections maintained in the facilities for deposition of microorganisms. As the result, they found that microorganisms of the genus Sphingomonas can accumulate very large amounts of biotin into the medium, thereby completing the present invention. Thus, the present invention provides a process for the production of biotin, characterized in that a microorganism of the genus Sphingomonas, having an ability to produce biotin, is cultured in an appropriate medium and biotin accumulated into the medium is collected. Also provided are microorganisms for use in this process. The microorganisms for use in the process of the present invention are those of the genus Sphingomonas , having an ability to produce biotin, examples of which are Sphingomonas adhaeshiva , Sphingomonas parapaucimobilis and Sphingomonas paucimonilis . Among these microorganisms, preferred is Sphingomonas sp. SC-42405. In general, the microorganisms of the genus Sphingomonas have, for example, the following characteristics: (1) They are gram-negative rods; (2) They exhibit positive in catalase test; (3) Yellow colonies are mainly formed; (4) They contain sphingolipids as phospholipids; (5) Isoprenoid quinone type is Q10; (6) They contain 2-hydroxy acids as bacterial fatty acids; and (7) The mol% G + C of their DNA ranges from about 60-70. Sphingomonas sp. SC-42405 is a microorganism which was isolated from the bacteria separated from the soil of Oita Prefecture, Japan, by the present inventors, and which was found to accumulate very large amounts of biotin in the medium. This microorganism has been deposited with the Fermentation Research Institute (renamed "National Institute of Bioscience and Human Technology") in the agency of Industrial Science and Technology, under the accession number of FERM BP-3995 on September 3, 1992, under the Budapest Treaty. The bacteriological characteristics of Sphingomonas sp. SC-42405 are as follows. (a) Morphology: 1. Shape and size of cells Shape: rods Size: 0.4-0.8 µm x 1.5-3.0 µm 2. Polymorphism: none 3. Motility: active, polar and peritrichous flagella 4. Sporulation: none 5. Gram staining: negative 6. Acid fastness: none (b) Growth properties: 1. Nutrient agar plate culture: round, convex, yellow 2. Nutrient agar slant culture: smooth surface, slightly glossy, yellow 3. Nutrient broth liquid culture: turbid growth 4. Nutrient broth gelatin stab culture: not liquefied 5. Litmus milk: not changed (c) Physiological properties: 1. Nitrate reduction (nutrient broth nitrate medium): - 2. Denitrification: - 3. MR test: - 4. VP test: - 5. Indole formation: - 6. hydrogen sulfide formation: + 7. Starch hydrolysis: - 8. Citrate utilization Koser medium: + Christensen medium: + 9. Inorganic nitrogen source utilization ammonium salts: + nitrates: + 10. Pigment formation Cellular pigments: + (yellow) Water-soluble pigments (King's A medium): - Water-soluble pigments (King's B medium): - 11. Urease: ± 12. Oxidase: + 13. Catalase: + 14. Growth conditions pH: 5.1-7.9 Temp.: 10-33°C 15. Attitude to oxygen: slightly aerobic 16. O-F test: F (weak) 17. Acid and gas formation from sugar Acid Gas (1) L-Arabinose: + - (2) D-Xylose: + - (3) D-Glucose: ± - (4) D-Mannose: ± - (5) D-Fructose: + - (6) D-Galactose: + - (7) Maltose: ± - (8) Sucrose: ± - (9) Lactose: ± - (10) Trehalose: - - (11) D-Sorbitol: - - (12) D-Mannitol: - - (13) Inositol: - - (14) Glycerol: - - (15) Starch: ± - (d) Other properties : 1. Aesculin hydrolysis: + 2. Arginine hydrolysis: - 3. Lysine decarboxylation: - 4. Ornithinedecarboxylation: - 5. DNase: - 6. Tween 80 hydrolysis: - 7. 0/129 Sensitivity: - 8. Nitrogenase: - 9. Poly-β-hydroxybutyrate accumulation: + 10. Mol% G + C of DNA: 64.8 11. Molecular type of isoprenoid quinone: ubiquinone Q10 12. Sphingophospholipids: + 13. Composition of total bacterial fatty acids: C16:0(13.1%), C16 : 1(11.2%), C17 : 1(1.1%), C18 : 1 (51.8%), 2-OH-14 : 0 (14.1%) and 2-OH-16 : 0 (4.5%) The above-described properties in the item (d), 10-13, can be determined by conventional chemotaxomonical procedures such as described in "Experiments for Identification of Actinomycetes", edited by the Japanese Society for the Research of Actinomycetes and published by the Secretariat of the Japanese Society for the Research of Actinomycetes in 1985. Typical examples of such procedures will be explained below. 1. Mol% G + C of DNA Culture (100 mL nutrient broth medium in Sakaguchi's flask at 30°C for 36 hrs.) Wash twice by centrifugation with saline-EDTA (0.15 M NaCl, 0.1 M EDTA, 8.0). Lysis of bacterial cells [lysozyme treatment (0.5 mg/mL at 37°C for 1 hr.), followed by addition of SDS (to final conc. of 12%) and heating at 60°C for 15 min.] Add EtOH to final conc. of 67%. Dissolve in 20 mL of SSC (0.15 M NaCl, 0.015 M Na 3 citrate, pH 7.0). Add phenol at equivalent volume to SSC (SSC saturation) and shake in stoppered flask. Pipette out water layer. Winding of DNA RNase treatment (add RNase A* to 50 µg/mL and treat at 37°C for 1 hr.) Winding of DNA around glass rod while adding EtOH (if pure DNA, it becomes transparent) Put 100 µL of purified DNA/0.1 X SSC solution into microcentrifugation tube. Reaction at 50°C for 1 hr. Reaction at 37 °C for 1 hr . HPLC analysis Column: Gµ C18+µBondasphere C18 (3.9 mm x 150 mm), Mobile phase: 0.2 M NH 4 H 2 PO 4 /MeOH (100:8), Flow rate: 0.9 mL/min., Detection: UV 260 nm, Sample injection: 5 µL (4-7 µL). 2. Molecular kind of isoprenoid quinone 100 mg of lyophilized bacterial cells (prepared as liquid culture in nutrient broth) Silica gel TLC analysis Scrape off in silica gel TLC and purification Remove by elution from silica gel with acetone Reverse phase HPLC analysis Column: YMC-Pack AM-303 (4.6 mm x 250 mm), Elute: 2-PrOH-MeOH(25 : 75), Flow rate: 1.0 mL/min., Detection: 270 nm. 3. Presence of sphingophospholipids 0.5 g of wet bacterial cells Separate CHCl 3 layer into two parts and add 88 µL of 6N KOH. TLC analysis (after development, color development is caused with molybdenum reagent.) 4. Composition of total bacterial fatty acids (1) Procedures for analysis of total bacterial fatty acids 25 mg of lyophilized bacterial cells (prepared as liquid culture in nutrient broth at 30°C) Let stand for cooling. Extract fatty acid methyl esters (shaking for 10 min.). . Dissolve in 200 µL of CH 3 CN. Gas chromatography analysis Column: 10% DEGS Chromosorb W 80/100 (AW-DMCS), 3 mm x 5.2 m, Carrier: N 2 at 40 mL/min., Injection temp.: 220°C, Column temp.: 180°C, Detection: FID. (2) Procedures for identification of unsaturated fatty acid methyl esters 20 µL of total bacterial fatty acid methyl ester sample Dissolve in 200 µL of ethyl ether. Evaporate solvent and remaining Br 2 by blowing N 2 gas. Gas chromatography analysis [in the same manner as described in item (1)] (3) Procedures for identification of hydroxy fatty acid methyl esters 20 µL of total bacterial fatty acid methyl ester sample Development ( n -hexane-ethyl ether, 85:15) Scrape off color-developed spots. Extract with ethyl ether, followed by dry up and dissolution in 20 µL of CH 3 CN. Gas chromatography [in the same manner as described in item (1)] (4) Procedures for identification of cyclo fatty acid methyl esters 20 µL of total bacterial fatty acid methyl ester sample Heat in 2 mL of 5% anhydrous HCI-MeOH at 100°C for 1 hr. Extract fatty acid methyl esters in the same manner as described in item (1) and dissolve in 20 µL of CH 3 CN. Gas chromatography analysis [in the same manner as described in item (1)] The above-described characteristics were compared with the data disclosed in "Bergey's Manual of Systematic Bacteriology" (1984), Yabuuchi et al., Microbiol. Immunol., 34, 99-119 (1990), Validation list No. 34, Int. J. Syst. Bacteriol., 40, 320-321 (1990), and the bacterial strain found by the present inventors was identified as a microorganism of the genus Sphingomonas and named Sphingomonas sp. SC-42405. It should be noted that there has not yet been known any microorganism of the genus Sphingomonas , having an ability to produce biotin. In this respect, Sphingomonas sp. SC-42405 is considered to be a novel strain. In addition, any variant of this strain, i.e., any mutant derived from Sphingomonas sp. SC-42405, any cell fusion strain or any recombinant strain is also available for the process of the present invention. A culture of the microorganism for use in the process of the present invention can be prepared in various kinds of media containing carbon and nitrogen sources, organic and/or inorganic salts, and the like, all of which have been widely used for preparing a culture of ordinary bacteria. Examples of the carbon sources are glucose, maltose, glycerol, starch, dextrin, sucrose, animal and vegetable oils, and molasses. Examples of the nitrogen source are natural organic nitrogen sources such as broth, peptone, yeast extract, malt extract, soy bean powder, corn steep liquor, cotton seed powder, dry yeast and casamino acid; and other organic or inorganic nitrogen sources such as ammonia, ammonium chloride, sodium nitrate, ammonium nitrate, ammonium sulfate, ammonium acetate and urea. The natural organic nitrogen sources may also be utilized as a carbon source. Examples of the organic and inorganic salts are chlorides, sulfates, acetates, carbonates and phosphates of elements such as potassium, sodium, magnesium, iron, manganese, cobalt and zinc. Specific examples thereof are potassium chloride, sodium chloride, magnesium sulfate, ferrous sulfate, manganese sulfate, cobalt chloride, zinc sulfate, copper sulfate, sodium acetate, calcium carbonate, sodium carbonate, potassium monohydrogenphosphate, potassium dihydrogenphosphate, sodium monohydrogenphosphate and sodium dihydrogenphosphate. The microorganism for use in the process of the present invention has a superior ability to produce biotin in various media which are favorable for the production on an industrial scale. To increase the ability to produce biotin for the microorganism used in the process of the present invention, an amino acid such as alanine or a fatty acid such as pimelic acid may be added to the culture medium. For example, these compounds may be used at an amount of from about 1 mg to about 5 mg per 1000 mL of the culture medium. A culture of the microorganism for use in the process of the present invention is prepared according to conventional procedures employed for ordinary bacteria, in the form of either a solid culture or a liquid culture such as shaking culture using test tubes, reciprocating shakers or rotary shakers, and other cultures using jar fermenters or fermentation tanks. A culture of the microorganism is usually incubated under aerobic conditions. In particular, when a jar fermenter or a fermentation tank is used, it is necessary to introduce aseptic air thereinto, usually at a rate of from about 0.1 to about 2 times the culture volume per minute. The incubation temperature may vary within a range in which the microorganism used is viable in culture. For example, the culture is incubated at a temperature of from about 20°C to about 40°C, preferably from about 25° to about 35°C, and more preferably from about 28° to about 33°C. Preferably, the medium pH is controlled at from about 6 to about 8. The incubation period may vary depending upon various conditions, and the culture is usually incubated over a period of from about 1 to about 7 days, preferably from about 3 to about 4 days. After completion of the incubation, biotin is collected from the culture by making use of the properties of biotin according to conventional procedures for extraction and purification of a desired compound from natural sources. For example, the bacterial cells are removed from the culture by a technique such as centrifugation, and biotin accumulated in the culture is adsorbed on activated charcoal or a macro-porous non-ionic exchange resin, followed by purification with an ion exchange resin or recrystallization utilizing a difference of solubility between biotin and impurities. The present invention will be further illustrated by way of the following examples which are not to be construed to limit the scope thereof. Example 1 Production of biotin by shaking culture A loopful of Sphingomonas sp. SC-42405 (FERM BP-3995) was inoculated into a large test tube (22 mm x 220 mm) containing 10 mL of pre-culture medium (1% glycerol, 2% polypeptone, 0.15% K 2 HPO 4 , 0.15% MgSO 4 ·7H 2 O, pH 7.2), and incubated at 30°C with shaking at 200 rpm for 3 days. Then, 2 mL of this pre-culture was inoculated into a 500 mL Sakaguchi's flask containing 50 mL of culture medium (2% glycerol, 2% yeast extract, 0.5% vitamin-free casamino acid, 0.15% K 2 HPO 4 , 0.05% KCl, 0.05% MgSO 4 ·7H 2 O, 0.001% FeSO 4 ·7H 2 O, 0.001% MnSO 4 ·4-6H 2 O, 20 µg/L thiamine hydrochloride, pH 7.0), and incubated at 30°C with shaking at 130 rpm for 4 days. The bacterial concentration (OD 650 ) after completion of the incubation was 22.0, at which time the concentration of biotin produced and accumulated in the medium was determined by quantitative microbial bioassay using Lactobacillus plantarum IFO 3070 (Izumi and Yamada, Methods of Vitaminological Experiments II, Water-soluble Vitamins, pp. 481-499, edited by the Vitaminological Society of Japan, Tokyo Kagaku Dohjin, 1985), and found to be 3.3 mg/L. Example 2 Production of biotin by aerobic stirring culture A culture of Sphingomonas sp. SC-42405 in a large test tube was pre-incubated in the same manner as described in Example 1. The pre-culture was inoculated as 2 mL portions into three 500 mL Sakaguchi's flasks each containing 100 mL of the same pre-culture medium, and incubated at 30°C with shaking at 130 rpm for 3 days. Then, 300 mL of this culture was inoculated into a 30 L jar fermenter containing 15 L of culture medium (2% glycerol, 2% yeast extract, 0.5% vitamin-free casamino acid, 0.15% K 2 HPO 4 , 0.05% KCl, 0.05% MgSO 4 ·7H 2 O, 0.001% FeSO 4 ·7H 2 O, 0.001% MnSO 4 ·4-6H 2 O, 20 µg/L thiamine hydrochloride, pH 7.0), and incubated at 30°C with aeration and stirring for 4 days. The rate of aeration was 15 L/min., and the rate of stirring was from 200 to 500 rpm (controlled so that the concentration of dissolved oxygen in the medium became 2 ppm or higher). The self-defoaming was achieved by addition of defoamer Einol (Biotto Co.). The bacterial concentration (OD 650 ) after completion of the incubation was 38.0, at which time the concentration of biotin produced and accumulated in the medium was determined by the same quantitative microbial bioassay as described in Example 1, and found to be 2.3 mg/L. Example 3 Isolation and Identification of products Fifteen liters of the culture obtained in Example 2 were subjected to continuous centrifugation, and after adjusted to pH 3 by addition of HCl, the supernatant was allowed to pass through a column packed with 500 g of activated carbon (Wako Pure Chemical Industries, Ltd.). The column was washed with 15 L of water, followed by elution with 5 L of 0.1 N ammonia water. The eluate was concentrated and allowed to pass through a column packed with 100 mL of Dowex 1 x 8 (The Dow Chemical Co.), followed by washing with 2 L of water and elution with 2 L of 1 N acetic acid. The eluate was concentrated and allowed to pass through a column packed with 100 mL of Dowex 50W-8 (The Dow Chemical Co.), followed by elution with 2 L of water. The eluate was concentrated and allowed to pass through a column packed with 50 g of activated carbon (Wako Pure Chemical Industries, Ltd.). The column was washed with 500 mL of water, followed by elution with 500 mL of 0.1 N ammonia water. The eluate was evaporated to dryness, and the residue was dissolved in 5 mL of 0.1 N aqueous sodium hydroxide, followed by purification through gel filtration chromatography using a column packed with 50 mL of Sephadex G-10 (Pharmacia AB). The fractions containing eluted biotin were combined and adjusted to pH 3 by addition of 0.05 N HCl, after which the combined fractions were allowed to stand overnight in a cool place. The precipitated crystals were collected and dried under reduced pressure, resulting in 13 mg of biotin crystals. The thus obtained biotin exhibited the same physicochemical properties (e.g., mass spectrum, infrared absorption spectrum) as those of the standard preparation of biotin. Example 4 Comparison of biotin production between various microorganisms A loopful of each of various microorganisms of the genus similar to the genus Sphingomonas was inoculated into a large test tube (22 mm x 220 mm) containing 5 mL of pre-culture medium (1% glycerol, 2% polypeptone, 0.15% K 2 HPO 4 , 0.15% MgSO 4 ·7H 2 O, pH 7.2), and incubated at 30°C with shaking at 250 rpm for 3 days. After completion of the incubation, the concentration of biotin produced and accumulated in the culture medium was determined by the same quantitative microbial bioassay as described in Example 1. The results are shown in Table 1. Microorganism Biotin production (µg/L) Growth at 30°C Flavobacterium flavescens JCM 7456 trace + Flavobacterium okeanokoites IFO 12536 trace + Pseudomonas auricularis IFO 13334 trace + Pseudomonas bathycetes JCM 6308 trace + Pseudomonas chlororaphis IFO 3904 trace + Pseudomonas diminuta JCM 2788 trace + Pseudomonas fluorescens IFO 14160 trace + Pseudomonas fragi IFO 3458 trace + Pseudomonas mucidolens JCM 2781 trace + Pseudomonas nitroreducens JCM 2782 trace + Pseudomonas oxalaticus IFO 13593 trace + Pseudomonas pertucinogena IFO 14163 trace + Pseudomonas putida IFO 14164 trace + Pseudomonas riboflavina IFO 13584 trace + Pseudomonas straminea JCM 2783 trace + Pseudomonas vesicularis JCM 1477 trace + Pseudomonas fluorescens trace + Pseudomonas aeruginosa trace + Pseudomonas taetrolens IFO 3460 trace + Sphingomonas adhaeshiva JCM 7370 2.3 + Sphingomonas parapaucimobilis JCM 7512 3.1 + Sphingomonas paucimobilis IFO 13935 9.8 + Sphingomonas paucimobilis IFO 13936 6.4 + Sphingomonas paucimobilis JCM 7509 5.8 + Sphingomonas paucimobilis JCM 7511 12.4 + Sphingomonas paucimobilis JCM 7515 13.7 + Sphingomonas paucimobilis JCM 7519 15.5 + Sphingomonas paucimobilis JCM 7521 9.5 + Sphingomonas sp. JCM 7513 2.7 + Sphingomonas sp. JCM 7514 4.2 + Sphingomonas sp. SC-42405 (FERM BP-3995) 17.4 + Xanthomonas campestris IFO 13551 ― - Xanthomonas maltophilia JCM 1975 ― -

Claims: A process for the production of biotin, comprising the steps of (a) preparing a culture of a microorganism of the genus Sphingomonas having an ability to produce biotin, in a medium; and (b) collecting biotin produced and accumulated in the medium. The process according to claim 1, wherein the microorganism of the genus Sphingomonas , having an ability to produce biotin, is Sphingomonas sp. SC-42405 (FERM BP-3995) or any variant, mutant, cell fusion strain or recombinant strain derived thereof. Use of a microorganism of the genus Sphingomonas , having an ability to produce biotin for producing biotin. The use of a microorganism for producing biotin according to claim 3, wherein the microorganism is Sphingomonas sp. SC-42405 (FERM BP-3995) or any variant, mutant, cell fusion strain or recombinant strain derived thereof. Sphingomonas sp. SC-42405 (FERM BP-3995) or any variant, mutant, cell fusion strain or recombinant strain derived thereof.

Inventors: KAWANO EMIKO, KUMAGAI KAZUO, MIKI MISAO, MITSUDA SATOSHI, KAWANO, EMIKO, KUMAGAI, KAZUO, MIKI, MISAO, MITSUDA, SATOSHI
Applicants: SUMITOMO CHEMICAL CO, SUMITOMO CHEMICAL COMPANY LIMITED
Application year: 1993
Main classification: C12P17
IPC codes: C12P17