• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    A new process of producing L-2-amino-4-(hydroxy­methylphosphinyl)-butyric acid (L-AMPB) is now provided, in which 4-(hydroxymethylphosphinyl)-2-oxo-butyric acid (OMPB) is treated with one or more transaminases or with one or more microorganisms capable of producing the transaminase, in the presence of one or more amino-donor compounds such as α-amino acids. According to this process, the optically active L-AMPB useful as herbicidal agent can be produced efficiently in a facile way for a reasonable reaction time.
    公开号:SU1731067A3
    申请号:SU874202766
    申请日:1987-06-08
    公开日:1992-04-30
    发明作者:Имаи Сатоси；Мураками Такеси；Хара Осаму；Миядо Синдзи；Кумада Еити；Анзаи Хироюки；Такане Нобухико；Есизава Ятие；Сайто Тосинори；Огава Хироси；Такеба Хидехи；Сато Ацуюки；Нагаока Козо；Фукацу Сунзо；Окада Акира
    申请人:Мейдзи Сейка, Лтд (Фирма)；
    IPC主号:
    专利说明:

    This invention relates to biotechnology and relates to a method for producing L-2-amino-4- (hydroxymethylphosphinyl) -buttonic acid having herbicidal activity that can be used as a herbicide.
    A known method for producing L-2-amino-4- (hydroxymethylphosphinyl) butyric acid of the formula
    ABOUT
    II
    CH3-p - CH2 CH2-CH-COOH
    he
    Bn
    including the cultivation of the producer strain of the specified acid, followed by isolation of the target product from the culture fluid.
    The disadvantage of this method is the long duration of the process, which makes it difficult to organize the industrial production of the product.
    The purpose of the invention is to accelerate the process.
    This goal is achieved by conducting the transamination of 4- (hydroxymethylphosphinyl) -2-oxobutyric acid in the presence of glutamic or aspar agonisic acid or their mixture as an NH2 donor and in the presence of glutamic acid - oxaloyane acetic acid transaminase or glutamic acid - pyro-grape acid transaminases, or their mixtures, or producer strains, indicated transaminases: Streptomyces hyjioscoplcus SF-1293 (PERM BP-130, AGCC 21705); Streptomyces hygroscoplcus NP-50 (PERM BP-1368); Streptomyces llvldans 66 (PERM BR-737); Streplomyces albus IFO 13014 (AT CC3004); Streptomyc3sgriseuslFO 12875 (ATCC 23345); Streptoverlcilllum cinnamoneum IFO 12852 (ATCC 11874), Streptomyces morookaensis IPO 13416 (ATCC I916P); Nocardia mediterranei ATCC 21271; Nocardiopsls dassonvlllel ICM 3237; Streptomyces vlridochromogenes IFO 13347 (ATCC14925); Streptomyces
    vlridochromogenesICM 4977;
    Mlcromonospora carbonaceae NRRL 2972 (ATCC 27114); Escherichla coll. ATCC 10798; Pseudomonas aeruglnosa ATCC 10145; Pseudomonas cepacla ATCC 17759; Serratia marcescens ATCC 13880; Candida albicans IAM 4888 or Mucor splnescens 1AM Mi 3 at pH 8.0-9.0, temperature 28-50 ° C and molar ratio of 4- (hydroxymethylphosphinyl) -2-oxo-butyric acid and NI-12 donor 1: 1-10.
    The method of obtaining amino acids by transamination of the corresponding oxoacids in the presence of glutamic or aspartic acids as MHA-donor and transaminase enzymes is known, however, to obtain | -2-amino- (hydroxymethylphosphinyl) -butyric acid is used for the first time.
    The method according to the invention is carried out as follows.
    4- {Hydroxymethylphosphinyl) -2-oxo-butyric acid is treated with at least
    at least one transaminase in the presence of at least one MH2-donor, for example, L-glutamic or L-aspartic acids or their mixture, in an aqueous medium, in
    which dissolved 4- (hydroxymethylphosphinyl) -2-oxo-butyric acid, MH2-donor and transaminase. The process is carried out at a pH of 8.0- 9.0 and a temperature of 28-50 ° C. The method can also be used by treating 4- (hydroxymethylphosphinyl) -2-oxomeric acid not by the transaminase itself, but by a strain of the microorganism capable of producing at least one transaminase. In this case, 4- (hydroxymethylphosphinyl) -2-oxobutyric acid and 1 H2-DONor are introduced into
    nutrient broth of a microorganism capable of producing a transaminase in which non-chemically affected cells of a strain of microorganism are suspended.
    The method can be carried out by treating 4- (hydroxymethylphosphinyl) -2-oxo-butyric acid with an extract of a microorganism capable of producing a transaminase containing this transaminase in the presence of an MH2 donor. No matter how
    the process is carried out in a manner that 4- (hydroxymethylphosphinyl) -2-oxo-butyric acid is dissolved with its initial concentration in an aqueous reaction medium of 0.1-100 mg / ml. The molar ratio of 4- (hydroxymethylphosphinyl) -2-oxobutyric acid and NH2-donor is from 1: 1-10 in the same reaction medium.
    When the reaction between 4- (hydroxymethylphosphinyl) -2-oxobutyric acid, H2donor and transaminase or cells of the transaminase producing microorganism strain of the invention is obtained, an aqueous reaction solution containing -2-amino-4- (hydroxymethylphosphinyl) -buttonic acid is obtained, unreacted 4- (hydroxymethylphosphinyl) -2-oxo-butyric acid, transaminase used or cells of the microorganism used. Before isolating the desired product from the reaction mixture, centrifugation was performed to isolate the cells of the microorganism used.
    Isolation and purification of the target product is carried out by passing the reaction
    mixtures through a cation exchange resin column, such as Dowex 50W, with which the target product is absorbed, after which it is eluted with water or with a dilute aqueous solution of ammonia.
    As a result, eluate fractions containing b2-amino-4- (hydroxymethylphosphinyl) butyric acid are obtained. Fractions
    the eluent is collected and concentrated under reduced pressure.
    Example. 4- (Hydroxymethylphosphine) -2-oxo-butyric acid is dissolved in 50 Mm of phosphate buffer solution (pH 6) containing glutamic acid — oxaloacetate acetic acid transaminase, L-aspartic and L-glutamic acid, serving as MH 2 donors.
    The process is conducted at 50 ° C for 50 minutes. The reaction mixture is then heated at 100 ° C for 3 minutes to complete the reaction. The pH of the reaction mixture is adjusted to 2 by the addition of a dilute aqueous solution of sulfuric acid and centrifuged to obtain a surface solution. The amount of the target product in the surface solution is determined by an amino acid analyzer.
    Example 2. Strains indicated in tab. 1, individually inoculated in 40 ml portions of a dilution medium including nutrient broth, followed by cultivation at 28 ° C for b h. The resulting nutrient broths are used for inoculation with an inoculum of 2% in 40 ml portions of the nutrient medium of the same composition and cultivation overnight at 28 ° C. 4- (hydroxymethylphosphinyl) -2-oxo-butyric acid is added to each of the obtained nutrient broths containing cells to a concentration of 100 µg / ml.
    Sodium salt of L-aspartic acid was introduced into each of the resulting broths as donor MH2 to a concentration of 00 μg / ml. Thereafter, enzymatic conversion is carried out, proceeding at 28 ° C for 24 hours. The pH of the resulting mixture is adjusted to 2 with 25% sulfuric acid to terminate the reaction. The cells are removed by centrifugation. The amounts of L-2-amino-4- (hydroxymethylphosphinyl) -butyric acid present in the surface solution are determined using an amino acid analyzer.
    The results of the summation in the table. one.
    EXAMPLE 3 A strain of Streptomyces hygroscoplcus SF-1293 (PERM BP-130) was inoculated in 10 ml of a preliminary dilution medium (including 2.0% soluble starch, 1.0% polypepton, 0.3% meat). extract, 0.05% potassium phosphate, pH 7.0), cultured at 28 ° C for 24 hours. The resulting nutrient broth is used as a seed culture and inoculated with
    the content of the inoculum 2% in a nutrient medium dilution, including,%: glucose 7; baktosiotone 4,4; potassium hydrogen phosphate 0.32; sodium hydrogen phosphate 0.0852, M-tris- (hydroxymethyl) methyl-2-aminoethanesulfonic acid 1.15; cobalt chloride 0.0001 (pH 6.0), and then the cultivation of strain SF-1293 at 28 ° C under anaerobic conditions and with stirring. After cultivation for 4 days, the microbial cells are removed by centrifugation and washed with 50 mM phosphate buffer (pH 6.0). These cells are then disintegrated by ultrasound treatment, followed by centrifugation to obtain a solution of the crude enzyme.
    4- (hydroxymethylphosphinyl) -2-oxo-butyric acid is added to this crude enzyme solution to a concentration of 100 µg / ml and L-aspartic acid to a concentration of 200 µg / ml. A control experiment was also carried out using 2-ketoglutaric acid as a control substrate for the transamination reaction. After the enzyme reaction was carried out at 30 ° C for 2 hours, the reaction solution was heated at 100 ° C for 3 minutes to complete the reaction.
    The pH of the resulting solution is adjusted to 2 with dilute sulfuric acid. A solution of the desired product is obtained by centrifuging this reaction solution. The amount of the target product and glutamic acid formed from ketoglutaric acid is determined using an amino acid analyzer.
    Get it. | -2-amino-4- (hydroxymethylphosphinyl) -button acid, 2.8 µg / ml; 2-KG glutamic acid 67.9 µg / ml (control).
    PRI me R 4. Use the strain Streptomyces hygroscopicus NP-50 (FERM P-7804).
    In a 250 ml Erlenmeyer flask, 20 ml of nutrient broth of Streptomyces hygroscopicus NP-50 strain, cultured for 3 days, 30 ml of an aqueous solution of 4- (hydroxymethylphosphinyl) -2-oxobutyric acid (concentration 87 mg / ml; pH 7 , 0), 40 ml of an aqueous solution of sodium L-glutamate (concentration 170 mg / ml) and 10 ml of a Tris-HCl molar buffer solution (pH 8.5). The process is carried out with gentle agitation of the mixture at 37 ° C for 24 hours. Then the reaction mixture is centrifuged to remove microbial cells from it, and the surface solution containing the desired product is analyzed using an amino acid analyzer. 14 mg / ml -2-amino-4- (hydroxymethylphosphine) -butyric acid are obtained.
    PRI me R 5. Use the strain Streptomyc.es livldans 66 (PERM BP-737).
    In a 250 ml Erlenmeyer flask, 20 ml of broth of Streptomyces livldans 66 strain, cultured for 3 days in a nutrient medium, 30 ml of an aqueous solution of 4- (hydroxymethylphosphinyl) -2-oxobutyric acid (concentration 87 mg / ml, pH 7.0), 40 ml of an aqueous solution of sodium L-glutamate (concentration 170 mg / ml) and 10 ml of 1 molar Tris-HCl buffer solution (pH 8.5). With gentle agitation of the resulting mixture at 37 ° C, an enzyme reaction is carried out, which proceeds for 24 hours. Then, the obtained reaction mixture is centrifuged to remove microbial cells from it. The resulting surface solution containing the L-2-amino-4- (hydroxymethylphosphinyl) -butyric acid (100 ml) formed is analyzed by means of an amino acid analyzer to determine the amount of the desired product. 6 mg / ml of 1 -2-amino-4- (hydroxymethylphosphinyl) butyric acid are obtained.
    Below are the results obtained using different strains of bacteria (Table 2), yeast (Table 3), actinomycetes (Table 4), fungi (Table 5), where is glutamic acid, Asp is asparaginic acid.
    In tab. 6 shows the results showing the dependence of the product yield on the concentration of the NH2-donor and the starting oxo-acid.
    权利要求:
    Claims (1)
    [1]
    Invention Formula
    The method of producing -2-amino-4- {hydroxymethylphosphinyl) -butyric acid of the formula Q
    w3-p-ch2-s1gg-sn soon
    Ii I
    onzsh.2
    characterized in that, in order to speed up the process, transamination of 4- (hydroxymethylphosphinyl) -2-hydroxyacid acid is carried out in the presence of glutamic or aspartic acid
    or their mixtures as MH2-donor and glutamic acid — well-terveous acetic acid transaminase or glutamic acid — pyruvic acid transaminase,
    or their mixtures, or producer strains of the indicated Streptomyces hygroscoplcus SF-1293 transaminases (PERM BP-130, ATCC 21705) or Streptomyces NP-50 hygroscopicus NP (PERM BP-1368), or Streptomyces
    livldans 66 (PERM BP-737), or Streptomyces albus IPO 13014 (ATCC 3004), or Streptomyces grlseus IPO 12875 (ATCC 23345), or Strepto-vlrlcllllum cinnamoneum IPO 12852 (ATCC 11874), or Streptomyces
    morookaensis IPO 13416 (ATCC 19166), or Nocardla mediterranei ATCC 21271, or Nocardlopsls dassonvlllel ICM 3237, or Streptomyces virldochromogenes ICM 4977, or Streptomyces viridochromogenes IPO
    13347 (ATCC 14925), or Mlcromonospora carbonaceae NRRL 2972 (ATCC 27114), or Esherlchia cofi ATCC 10798, or Pseudomonas aeruglnosa ATCC 10145, or Pseudomonas cepacie ATCC 17759, or
    Serratla marcescens ATCC 13880, or Candida alblcans IAM 4829, or Mucor spinescens IAM MiZ at pH 8.0-9.0, temperature 28-50 ° С and molar ratio of 4- (hydroxymethylphosphinyl) -2-oxo-butyric acid and NH2- flOHopa 1: 1-10.
    The priority in paragraphs 9.04.86: transamination of 4- (hydroxymethylphosphinyl) -2-oxo-butyric acid is carried out in the presence of glutamic acid — oxaloacetic acid transaminase or glutamic acid — pyruvic acid transaminase, or mixtures thereof, or the producing strains of these transaminase, SF-1293 ATCC
    10145, ATCC 13880, ATCC 9341.
    01/23/87: in the presence of glutamic acid as MH2-donor, strains NP-50-FERMBP-737.
    03/30/87: in the presence of producer strains of the indicated transaminases IFO 13014, IFO 12875, IFO 12852, IFO 13416, ATCC 21271, ICM 3237, ICM 4977, IFO 13347. NRRL 2972, ATCC 17759, AM 4829, AM MiZ.
    25.04.87: in the presence of esparagin
    acids as MH2 donor or mixtures thereof.
    Table 1
    The yield of the product depending on the strain
    The yield of the product when using bacteria
    The yield of the product when using yeast
    The product yield when using actinomycetes
    Streptomyces albus IFO 13014 (ATCC 3004)
    Streptomyces griseus IFO 12075 (ATCC 23345)
    Streptovericilliumi cinnanioneum IFO 12852 (ATCC 11874)
    Streptomyces morookaensis IFO 13416 (ATCC 19166)
    Nocardia mediterranei ATCC 21271 Nocardiopsis dassonvillei ICM 3237
    Streptomyces viridochromogenes IFO 13347 (ATCC 14925)
    Micromonopora carbonaceae NRRL 2972 (ATCC 27114)
    Streptomyces viridochromogenes ICM 4977
    table 2
    Table 3
    Table
    t, 6
    1, 5.6
    The yield of the product when using mushrooms
    8.5.
    Note: Run 9 was performed at 50 ° C and pH 9.0, and Run 11 at 45 ° C and pH
    Table 5
    Table 6
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    同族专利:
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    IN165699B|1989-12-16|
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    EP0249188A3|1989-01-25|
    ES2059324T3|1994-11-16|
    NZ220576A|1990-05-28|
    EP0249188B1|1994-09-14|
    HUT46698A|1988-11-28|
    KR940005654B1|1994-06-22|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    JP13174386|1986-06-09|
    JP1251387|1987-01-23|
    JP7447687|1987-03-30|
    JP10115287|1987-04-25|
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