Process for producing optically active 1,3-butanediol

Abstract: Optically active 1,3-butanediol can be obtained by treating an enantiomer mixture of 1,3-butanediol with a microorganism or its treated one, capable of acting on the enantiomer mixture of 1,3-butanediol so as to leave (R)- or (S)-1,3-butanediol as such. Further, optically active 1,3-butanediol can be obtained by treating 4-hydroxy-2-butanone with a microorganism or its treated one, capable of asymmetrically reducing the 4-hydroxy-2-butanone into (R)- or (S)-1,3-butanediol.

Description: [Field of the Invention] This invention relates to a process for producing optically active 1,3-butanediol. More particularly, it relates to a process for producing optically active 1,3-butanediol which comprises treating an enantiomer mixture of 1,3-butanediol with a specific microorganism or its treated one, and recovering the remaining optically active 1,3-butanediol. Optically active 1,3-butanediols are important materials for synthesizing various drugs such as antibiotics. They are further usable as starting materials for synthesizing azetidinone derivatives, which are intermediate materials for tenem and carbapenem antibiotics, as well as various drugs and agricultural chemicals. [Prior Art] Known examples of the processes for producing optically active 1,3-butanediol include (1) one comprising resolving a racemic modification of 1,3-butanediol synthesized chemically by using an agent for optical resolution (Japanese Patent Laid-Open No. 191631/1986); and (2) another one comprising asymmetrically synthesizing from 4-hydroxy-2-butanone by using a Raney nickel catalyst which has been treated with an optically active compound [Japanese Patent Laid-Open No. 204187/1983 and Bull. Chem. Soc. Jpn., 53 , 1356 - 1360 (1980)]. However, it is disadvantageous that each of these processes (1) and (2) requires the use of an expensive agent for optical resolution or an expensive catalyst, and that, further, the process (2) gives only a poor optical purity. Accordingly, it has been urgently required to establish a process for economically and conveniently producing optically active 1,3-butanediol having a high optical purity. In addition, there have been reported some processes for producing optically active 1,3-butanediol by using a microorganism [refer to, for example, WO 89/10410 corresponding to EP Application 89-905185 and US Serial No. 449929; Levene and A. Walti, J. Bioi. Chem., 94 (1931) P.A. 361 - 366; and Carl Neuberg and Elisabeth Kub, Biochem. Z., 92 (1918), 96 - 110]. Japanese Patent Laid-Open No. 31684/1991 describes a process for producing optically active 1,3-butanediol through the asymmetrical reduction with a certain microorganism. Japanese patent application JP-A-1-320997 (Patent Abstracts of Japan Vol. 14, No. 123 (C-0698) 08.03.90) relates to a process for producing (R)-1,3-butanediol by treating an enantiomeric mixture of 1,3-butanediol with a microorganism selected from the genera Arthroascus, Candida, Debaryomyces, Endomyces , Guilliermondella, Hansenula, Kluyveromyces and Lodderomyces. WO 89/10410 relates to a process for producing (R)-1,3-butanediol by treating an enantiomeric mixture of 1,3-butanediol with a microorganism selected from the genera Brevibacterium, Candida, Enterobacter, Geotrichium, Klebsiella, Lodderomyces, Pseudomonas, Rhodotorula, Saccharomyces, Saccharomycopsis, Sterigmatomyces and Trichosporon. [Disclosure of the Invention] The present inventors have given their attention to a process for economically and conveniently producing optically active 1,3-butanediol of a high optical purity by using a microorganism and attempted to search for microorganisms suitable for this purpose. As a result, they have found out that a microorganism selected from those belonging to the genus Streptomyces acts on an enantiomer mixture of 1,3-butanediol so as to leave (R)-1,3-butanediol as such, thus completing the present invention. In a preferred embodiment said microorganism belongs to the species Streptomyces netropsis. These microorganisms may be suitably used in the present invention regardless of form (i.e., wild strains, mutants or recombinants obtained through genetic engineering techniques such as cell fusion or gene recombination). Microorganisms to which IFO Nos. are assigned are described in List of Cultures, 8th ed., Vol. 1 (1988) published by institute for Fermentation, Osaka (IFO) and available therefrom. Any medium may be used for incubating the microorganism to be used in the present invention, so long as the microorganism can grow therein. Thus any carbon source the microorganism is available (for example, sugars such as glucose, fructose, sucrose and dextrin, alcohols such as sorbitol, ethanol and glycerol, organic acids such as fumaric acid, citric acid, acetic acid and propionic acid and salts thereof, hydrocarbons such as paraffin and mixtures thereof) may be used. A nitrogen source, for example, ammonium salts of inorganic acids such as ammonium chloride, ammonium sulfate and ammonium phosphate, ammonium salts of organic acids such as ammonium fumarate and ammonium citrate, inorganic or organic nitrogenous materials such as meat extract, yeast extract, corn steep liquor, casein hydrolysate and urea and mixtures thereof may be used. The medium may further contain nutritional sources commonly employed for culturing microorganisms, for example, inorganic salts, trace metal salts and vitamins. Furthermore, factors for promoting the growth of the microorganism, those for elevating the productivity of the target compound and materials effective in maintaining the pH value of the medium at a desired level may be added thereto, if required. The microorganism may be incubated at a medium pH value of from 3.0 to 9.5 (preferably from 4 to 8) at an incubation temperature of from 20 to 45°C (preferably from 25 to 37°C) under such conditions (aerobic or anaerobic) as to suit the growth of the microorganism for from 5 to 120 hours (preferably from 12 to 72 hours). A means for preparing optically active 1,3-butanediol from the enantiomer mixture of 1,3-butanediol includes a method of using the culture medium as such and adding the enantiomer mixture of 1,3-butanediol thereto, and a method that the cells are separated by, for example, centrifugation, optionally washed and-then suspended in a buffer solution or water and the enantiomer mixture of 1,3-butanediol is added to the resulting suspension and is reacted. It is sometimes advantageous to add a carbon source, for example, glucose or sucrose to the reaction mixture as an energy source. The cells may be used either in the form of viable cells or in a treated state (for example, as ground, acetone-treated or lyophilized cells). These cells or treated cells may be used as immobilized form obtained by a known method (for example, polyacrylamide gel method, sulfur-containing polysaccharide gel methods such as carageenan gel method, alginic acid gel method or agar gel method). Furthermore, enzymes obtained from the treated cells by combining known purifying techniques may be used therefor. The enantiomer mixture of 1,3-butanediol may be used either as such or dissolved in water or an inert organic solvent or dispersed in, for example, a surfactant. The whole enantiomer mixture may be added at once at the initiation of the reaction, or alternately it may be added in portions. The reaction may be effected within a pH range of from 3 to 10 (preferably from 5 to 9) at a temperature of from 10 to 60°C (preferably from 20 to 40°C) for 1 to 120 hours under stirring or allowing to stand. Optically active 1,3-butanediol of a higher optical purity can be obtained by prolonging the reaction period, though the amount of the remaining 1,3-butanediol is decreased thereby. The concentration of the substrate may preferably range from 0.1 to 10%, though the present invention is not restricted thereby. The remaining optically active 1,3-butanediol may be easily recovered by a common purifying technique (for example, extraction with an organic solvent, distillation or column chromatography) either directly from the reaction mixture or after separating the cells. Particular examples of the microorganism capable of acting on an enantiomer mixture of 1,3-butanediol so as to leave (R)-1,3-butanediol as such include Streptomyces netropsis HUT 6068. These microorganisms may be suitably used in the present invention regardless of form (i.e., wild strains, mutants or recombinants obtained through genetic engineering techniques such as cell fusion or gene recombination). Microorganisms to which JCM Nos. are assigned are described in Catalog of Strains, 4th ed. (1989) published by Japan Collection of Microorganisms, RIKEN and available therefrom. Those to which DSM Nos. are assigned are described in Catalog of Srains (1989) published by Deatsche Sammlung von Mikroorganismen (DSM) and available therefrom. Those to which HUT Nos. are assigned are available from Department of Fermentation Engineering, Faculty of Technology, Hiroshima University. Microorganisms to which IFO Nos. are assigned are described in List of Cultures, 8th ed., Vol. 1 (1988) published by Institute for Fermentation, Osaka (IFO) and available therefrom. Those to which AHU Nos. are assigned are described in Catalogue of Cultures, 4th ed. (1987) published by Japanese Federation of Culture Collections of Microorganisms (JFCC) and available from Faculty of Agriculture, Hokkaido University. Those to which JCM Nos. are assigned are described in Catalog of Strains, 3rd ed. (1986) published by Japan Collection of Microorganisms, RIKEN and available therefrom. Those to which ATCC Nos. are assigned are described in Catalogue of Bacteria Phages rDNA Vectors, 16th ed. (1985) and Catalogue of Fungi/Yeast, 17th Ed. (1987) published by American Type Culture Collection (ATCC) and available therefrom. Those to which DSM Nos. are assigned are described in Catalog ofstrains (1983) published by Deutsch Sammlungvon Mikroorganismen (DSM) and available therefrom. Those to which IAM Nos. are assigned are available from Institute of Applied Microbiology, the University of Tokyo. [Examples] To further illustrate the present invention, and not by way of limitation, the following Examples will be given. In each Example, 1,3-butanediol in the reaction mixture could be easily determined by gas chromatography [column: Thermon 3000, 2m, temperature: 130°C), while the optical purity was measured by acetylating the obtained optically active 1,3-butanediol with the use of acetyl chloride by a conventional method and then subjecting to high-performance liquid chromatography by using an optical resolution column (column: Chiralcel OB produced by Daicel Chemical Industries, Ltd., solvent: n-hexane/2-propanol (19 : 1), wavelength: 220 nm, flow rate: 0.5 ml/min.) (retention time of (S)-form: 15 minutes, that of (R)-form: 19.3 minutes). Comparative Example 1 Medium for preparing cells: glucose 1.0% yeast extract 0.3% peptone 0.5% 1,3-butanediol 0.5% K 2 HPO 4 0.1% MgSO 4 ·7H 2 O 0.05% pH 7.2. 100 ml of the above-mentioned medium for preparing cells was introduced into a 500-ml Sakaguchi flask and sterilized. Then the medium was inoculated with each microorganism listed in Table 1. After incubating under shaking at 30°C for 48 hours, the cells were separated by centrifugation and washed with physiological saline once. Thus viable cells were obtained. Next, 50-ml of distilled water was introduced into a 500 ml Sakaguchi flask and the above-mentioned viable cells were suspended therein. 0.5 g of 1,3-butanediol in a racemic modification was added thereto and the mixture was incubated under reciprocal shaking at 30°C for 48 hours. After the completion of the reaction, the cells were removed by centrifugation. Then the obtained supernatant was saturated with sodium chloride and extracted with 50-ml of ethyl acetate. The ethyl acetate layer was analyzed by gas chromatography and thus the remaining 1,3-butanediol was determined. Next, the ethyl acetate was dehydrated over anhydrous sodium sulfate. After solvent removal, the obtained syrup was acetylated with acetyl chloride by a conventional method, dissolved in a solvent and analyzed by high performance liquid chromatography to determine the absolute configuration and optical purity of the 1,3-butanediol thus obtained. Table 1 summarizes the results. Microorganism Remaining 1,3-butanediol (mg/ml) Absolute configuration Optical purity of 1,3-butanediol (% e.e.) Clavispora lusitaniae IFO 1019 3.7 R 43 Kloeckera africana IFO 0869 8.7 R 48 Schizoblastosporion kobayashii IFO 1644 4.5 R 87 Eremascus fertilis IFO 0691 3.6 S 90 Syringospora claussenii IFO 0759 0.2 S 61 Sporopachydermia lactativora IFO 1867 0.1 S 95 Zygoascus hellenicus IFO 1575 4.1 S 98 Zygozyma oligophaga IFO 10360 0.2 S 99 Example 2 Medium for preparing cells: bonito meat extract 1.0% polypeptone 1.0% sodium chloride 0.5% pH 7.3. 100 ml of the above-mentioned medium for preparing cells was introduced into a 500-ml Sakaguchi flask and sterilized. Then the medium was inoculated with each microorganism listed in Table 2. After incubating under shaking at 30°C for 48 hours, the cells were separated by centrifugation and washed with physiological saline once. Thus viable cells were obtained. Next, 50 ml of distilled water was introduced into a 500-ml Sakaguchi flask and the above-mentioned viable cells were suspended therein. 0.5 g of 1,3-butanediol in a racemic modification was added thereto and the mixture was incubated under reciprocal shaking at 30°C for 48 hours. After the completion of the reaction, the cells were removed by centrifugation. Then the obtained supernatant was saturated with sodium chloride and extracted with 50 ml of ethyl acetate. The ethyl acetate layer was analyzed by gas chromatography and thus the remaining 1,3-butanediol was determined. Next, the ethyl acetate was dehydrated over anhydrous sodium sulfate. After solvent removal, the obtained syrup was acetylated with acetyl chloride by a conventional method, dissolved in a solvent and analyzed by high performance liquid chromatography to determine the absolute configuration and optical purity of the 1,3-butanediol thus obtained. Table 2 summarizes the results. Microorganism Absolute configuration Optical purity (% e.e.) Remaining 1,3-butanediol (mg/ml) Rhodococcus erythropolis DSM 43200 R 90 4.3 Rhodococcus erythropolis JCM 2893 R 80 4.5 Rhodococcus rubropertinctus DSM 43346 R 89 5.1 Rhodococcus rhodochrous JCM 2157 R 71 4.0 Rhococcus equi JCM 1311 R 71 3.8 Gordona bronchialis JCM 3198 R 77 3.3 Streptomyces netropsis HUT 6068 R 51 6.5 Rhodococcus rhodochrous DSM 43273 S 60 6.3 Rhodococcus erythropolis DSM 43274 S 58 6.4 Rhodococcus roseus JCM 2158 S 53 6.3 Gordona sputi JCM 3228 S 56 6.0 Comparative Example 3 A YM medium comprising 0.3% of yeast extract, 0.3% of malt extract, 0.5% of peptone and 2% of glucose (pH: 6.0) was used for strains of yeast like fungi, while a YPM medium comprising 2% of glucose, 0.5% of yeast extract, 0.3% of peptone, 0.3% of meat extract, 0.2% of (NH 4 ) 2 HPO 4 and 0.1% of KH 2 PO 4 (pH: 7) was used for strains of bacteria. 100 ml of each medium was introduced into a 500-ml Sakaguchi flask and sterilized. Then the medium was inoculated with each microorganism listed in Table 3. After incubating under reciprocal shaking at 27°C for 48 hours, the cells were separated by centrifugation and washed with physiological saline once. Thus viable cells were obtained. Next, 50-ml of distilled water was introduced into a 500 ml Sakaguchi flask and the above-mentioned viable cells were suspended therein. 5 g of glucose was added to the obtained suspension followed by reciprocal shaking at 27°C for 10 minutes. Then 0.5 g of 4-hydroxy-2-butanone was added thereto and the mixture was incubated under reciprocal shaking at 27°C for 20 hours. After the completion of the reaction, the cells were removed by centrifugation. Then the obtained supernatant was saturated with sodium chloride and extracted with 50 ml of ethyl acetate. The ethyl acetate layer was analyzed by gas chromatography to examine the reaction yield. Next, the ethyl acetate layer was dehydrated over anhydrous sodium sulfate. After solvent removal, the obtained syrup was acetylated with acetyl chloride by a conventional method, dissolved in a solvent and analyzed by high performance liquid chromatography to determine the absolute configuration and optical purity of the product. Table 3 summarizes the results. Microorganism Reaction yield (%) Absolute configuration Optical purity (% e.e.) Agrobacterium radiobacter IFO 12664 27 R 41 Azotobacter chroococcum IFO 12994 44 R 53 Bordetella bronchiseptica IFO 13691 33 R 40 Brettanomyces abstines DSM 70726 42 R 66 Dekkera bruxellensis IFO 1590 51 R 54 Endomyces decipiens IFO 0102 38 R 40 Eremascus fertilis IFO 0691 34 R 38 Erwinia carotovora subsp. carotovora IFO 3830 25 R 51 Fusarium oxysporum IFO 7152 85 R 95 Fusarium soiani IFO 5232 91 R 96 Geotrichum fragrans JCM 1749 62 R 60 Gibberella fujikuroi IFO 5268 55 R 42 Glomerella cingulata IAM 8050 47 R 90 Gonatobotryum apiculatum IFO 9098 39 R 44 Klebsiella pneumoniae IFO 12059 49 R 35 Micrococcus luteus IFO 3333 47 R 37 Micrococcus roseus IFO 3764 51 R 41 Mycobacterium smegmatis IFO 3153 50 R 40 Neosartorya fischeri var. spinosa IFO 5955 39 R 88 Oospora astringenes IFO 7001 41 R 53 Pachysolen tannophilus IFO 1007 47 R 61 Paecilomyces variotii IFO 4855 53 R 55 Paracoccus denitrificans IFO 12442 56 R 37 Preussia terricola IFO 7893 42 R 42 Saccharomyces cerevisiae IAM 0216 45 R 47 Saccharomycopsis fibuligera IFO 0103 58 R 60 Serratia marcescens IAM 1105 32 R 37 Syringospora claussenii IFO 0759 41 R 58 Spetoria glycines IFO 5294 53 R 54 Sporopachydermia lactativora IFO 1867 78 R 95 Talaromyces flavas var. flavas IFO 7231 48 R 47 Westerdykella multispora IFO 5813 48 R 42 Zygoascus hellenicus IFO 1575 81 R 97 Zygozyma oligophaga IFO 10360 88 R 95 Aciculoconidium aculeatum IFO 10124 45 S 56 Brettanomyces anonalus IFO 0796 44 S 61 Clavispora lusitaniae IFO 1019 51 S 48 Cochliobolus miyabeanus IFO 6631 45 S 55 Corynespora cassiicola IFO 6724 58 S 61 Dactylium dentroides ATCC 46032 43 S 65 Echinopodospora jamaicensis IFO 9819 40 S 70 Enterobacter cloacae ATCC 7256 40 S 51 Hamigera avellanea IFO 7721 43 S 57 Helminthosporium sigmoideum var. irregulare IFO 5273 50 S 53 Kloeckera africana IFO 0869 60 S 65 Nectria cinnabarina IFO 6821 44 S 48 Pseudomonas diminuta IFO 12697 41 S 50 Phialocephala bactrospora IFO 8770 55 S 45 Rhodotorula glutinis IFO 0395 42 S 53 Saccharomyces cerevisiae AHU 3402 38 S 55 Sterigmatomyces elviae DSM 70852 53 S 60 Schizoblastosporion kobayasii IFO 1644 71 S 95

Claims: A process for producing optically active 1,3-butanediol comprising treating an enantiomer mixture of 1,3-butanediol with a microorganism which may be ground, acetone-treated, lyophilized or immobilized, selected from among those belonging to the genus Streptomyces and capable of acting on an enantiomer mixture of 1,3-butanediol so as to leave (R)-1,3-butanediol as such and collecting the remaining optically active (R)-1,3-butanediol. The process of claim 1 wherein said microorganism belongs to the species Streptomyces netropsis.

Inventors: KOBAYASHI YOSHINORI, MATSUYAMA AKINOBU, KOBAYASHI, YOSHINORI, MATSUYAMA, AKINOBU
Applicants: DAICEL CHEM, DAICEL CHEMICAL INDUSTRIES, LTD.
Application year: 1991
Main classification: C12P7
IPC codes: C12P41