JPH036139B2 - - Google Patents
Info
- Publication number
- JPH036139B2 JPH036139B2 JP57192674A JP19267482A JPH036139B2 JP H036139 B2 JPH036139 B2 JP H036139B2 JP 57192674 A JP57192674 A JP 57192674A JP 19267482 A JP19267482 A JP 19267482A JP H036139 B2 JPH036139 B2 JP H036139B2
- Authority
- JP
- Japan
- Prior art keywords
- abscisic acid
- cis
- trans
- resin
- organic solvent
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- JLIDBLDQVAYHNE-YKALOCIXSA-N (+)-Abscisic acid Chemical compound OC(=O)/C=C(/C)\C=C\[C@@]1(O)C(C)=CC(=O)CC1(C)C JLIDBLDQVAYHNE-YKALOCIXSA-N 0.000 claims description 86
- FCRACOPGPMPSHN-UHFFFAOYSA-N desoxyabscisic acid Natural products OC(=O)C=C(C)C=CC1C(C)=CC(=O)CC1(C)C FCRACOPGPMPSHN-UHFFFAOYSA-N 0.000 claims description 43
- 239000003960 organic solvent Substances 0.000 claims description 15
- 239000011347 resin Substances 0.000 claims description 14
- 229920005989 resin Polymers 0.000 claims description 14
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 12
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 9
- 239000003957 anion exchange resin Substances 0.000 claims description 9
- 239000003480 eluent Substances 0.000 claims description 9
- 238000000034 method Methods 0.000 claims description 9
- 239000004793 Polystyrene Substances 0.000 claims description 8
- 229920002223 polystyrene Polymers 0.000 claims description 8
- 238000001179 sorption measurement Methods 0.000 claims description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 6
- 238000010828 elution Methods 0.000 claims description 5
- 239000000126 substance Substances 0.000 claims description 5
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 claims description 4
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 claims description 3
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 21
- 239000000243 solution Substances 0.000 description 15
- 239000000047 product Substances 0.000 description 10
- 239000007788 liquid Substances 0.000 description 9
- 229920001467 poly(styrenesulfonates) Polymers 0.000 description 7
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- 239000013078 crystal Substances 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 229920001817 Agar Polymers 0.000 description 5
- 241001064001 Rosisphaerella rosicola Species 0.000 description 5
- 239000002253 acid Substances 0.000 description 5
- 239000008272 agar Substances 0.000 description 5
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 4
- 239000002609 medium Substances 0.000 description 4
- 239000003513 alkali Substances 0.000 description 3
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 3
- 239000001965 potato dextrose agar Substances 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 229920001429 chelating resin Polymers 0.000 description 2
- 238000000855 fermentation Methods 0.000 description 2
- 230000004151 fermentation Effects 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 239000003456 ion exchange resin Substances 0.000 description 2
- 229920003303 ion-exchange polymer Polymers 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 235000010755 mineral Nutrition 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000011218 seed culture Methods 0.000 description 2
- 229910052938 sodium sulfate Inorganic materials 0.000 description 2
- 235000011152 sodium sulphate Nutrition 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000000638 solvent extraction Methods 0.000 description 2
- -1 ~2N Substances 0.000 description 2
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 1
- 241000351221 Alternaria rosicola Species 0.000 description 1
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 1
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 1
- 235000011130 ammonium sulphate Nutrition 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- FUKUFMFMCZIRNT-UHFFFAOYSA-N hydron;methanol;chloride Chemical compound Cl.OC FUKUFMFMCZIRNT-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003375 plant hormone Substances 0.000 description 1
- 229940072033 potash Drugs 0.000 description 1
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 1
- 235000015320 potassium carbonate Nutrition 0.000 description 1
- OVARTBFNCCXQKS-UHFFFAOYSA-N propan-2-one;hydrate Chemical compound O.CC(C)=O OVARTBFNCCXQKS-UHFFFAOYSA-N 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Description
【発明の詳細な説明】
本発明は(+)シス−トランス型アブサイジン
酸(以下アブサイジン酸と略記する)の精製法に
関する。さらに詳細には、本発明は強塩基性陰イ
オン交換樹脂またはポリスチレン系多孔性吸着樹
脂を用いる(+)シス−トランス型アブサイジン
酸の精製法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for purifying (+) cis-trans abscisic acid (hereinafter abbreviated as abscisic acid). More specifically, the present invention relates to a method for purifying (+) cis-trans type abscisic acid using a strongly basic anion exchange resin or a polystyrene-based porous adsorption resin.
アブサイジン酸は天然型植物ホルモンとして重
要なものであり、広い使途が期待されている。 Abscisic acid is an important natural plant hormone and is expected to have a wide range of uses.
従来発酵法によるアブサイジン酸の生成につい
ては、セルコスポラ・ロシコラ(Cercospora
rosicola)による固体培養および液体静置光照射
培養が知られているが、アブサイジン酸の生成量
は少なく培養期間は30〜40日の長期を要し、工業
的には難点があつた。また培養物・培養液からア
ブサイジン酸を精製単離する方法としては、酢酸
エチル等水に溶けにくい有機溶媒を加え、有機溶
媒層に抽出させ精製する方法が知られているが、
多量の有機溶媒を使用するため、工業的にはやは
り難点があつた。(Experientia 33 1556 1977
年)。 For the production of abscisic acid by conventional fermentation methods, Cercospora rosicola
Solid culture and liquid stationary light irradiation culture using A. rosicola) are known, but the amount of abscisic acid produced is small and the culture period requires a long period of 30 to 40 days, which is difficult from an industrial perspective. In addition, a known method for purifying and isolating abscisic acid from culture materials and broth is to add an organic solvent that is not soluble in water, such as ethyl acetate, and extract it into the organic solvent layer for purification.
Since a large amount of organic solvent is used, it is still difficult from an industrial perspective. (Experientia 33 1556 1977
Year).
最近上述のセルコスポラ・ロシコラによる通気
撹拌液体探部培養が見出され、培養期間15〜20日
で培養液中にアブサイジン酸が60μg/ml以上蓄
積することが明らかにされ、工業化が可能となつ
た。また培養液からのアブサイジン酸の精製単離
は従来知られていた溶媒抽出の他にイオン交換樹
脂による方法を用いることができることが明らか
となつた(特開昭56−160996)。 Recently, the above-mentioned aerated agitation liquid probe culture of Cercospora rosicola was discovered, and it was revealed that more than 60 μg/ml of abscisic acid was accumulated in the culture solution after 15 to 20 days of culture, making industrialization possible. . Furthermore, it has become clear that abscisic acid can be purified and isolated from a culture solution by using a method using an ion exchange resin in addition to the conventionally known solvent extraction (Japanese Patent Application Laid-Open No. 160996/1983).
しかし溶媒抽出は多量の溶媒を使用する難点が
あり、イオン交換樹脂を用いる常法では極めて収
率が悪い欠点があつた。 However, solvent extraction has the drawback of using a large amount of solvent, and conventional methods using ion exchange resins have the drawback of extremely low yields.
そこで本発明者らは、培養液からアブサイジン
酸を工業的な規模で精製する方法を種々検討し
た。この結果強塩基性陰イオン交換樹脂またはポ
リスチレン系多孔性吸着樹脂にアブサイジン酸を
含む培養液を接触させることにより、これらの
樹脂にアブサイジン酸を吸着させ、強塩基性陰イ
オン交換樹脂に吸着したアブサイジン酸はメタノ
ール,アセトン等の水溶性有機溶媒を含んだ酸ま
たはアルカリまたは塩により、またポリスチレン
系多孔性吸着樹脂に吸着したアブサイジン酸は該
樹脂を使用する場合に用いられる一般的な溶出剤
により、収率よく回収できることを見出し本発明
を完成するに至つた。 Therefore, the present inventors investigated various methods for purifying abscisic acid from a culture solution on an industrial scale. As a result, by contacting a culture solution containing absisic acid with a strongly basic anion exchange resin or a polystyrene-based porous adsorption resin, abscisic acid is adsorbed on these resins, and abscisin adsorbed on the strongly basic anion exchange resin is absorbed. The acid is treated with an acid or alkali or salt containing a water-soluble organic solvent such as methanol or acetone, and the abscisic acid adsorbed on a polystyrene-based porous adsorption resin is treated with a general eluent used when using the resin. They found that it can be recovered in good yield and completed the present invention.
従来、アブサイジン酸の精製に際しこれら強塩
基性陰イオン交換樹脂による方法は知られている
が〔特開昭56−160996〕溶出剤に水溶性有機溶媒
を含むものを使用すれば溶出率を著しく高めるこ
とができることについては知られておらず、更に
ポリスチレン系多孔性吸着樹脂を使用した例はま
つたく知られていない。 Conventionally, methods using strong basic anion exchange resins have been known for the purification of abscisic acid, but the elution rate can be significantly increased if an eluent containing a water-soluble organic solvent is used [JP-A-56-160996]. It is not known that this is possible, and furthermore, there are no known examples of using polystyrene-based porous adsorption resins.
以下本発明を詳細に説明する。 The present invention will be explained in detail below.
本発明によれば、アブサイジン酸を含む溶液を
強塩基性陰イオン交換樹脂またはポリスチレン系
多孔性吸着樹脂と接触させることにより、アブサ
イジン酸を該樹脂に吸着させ、しかる後に溶出剤
により溶出することによりアブサイジン酸を精製
することができる。 According to the present invention, abscisic acid is adsorbed onto the resin by contacting a solution containing abscisic acid with a strongly basic anion exchange resin or a porous polystyrene adsorption resin, and then eluted with an eluent. Abscisic acid can be purified.
アブサイジン酸を含む溶液は、たとえばセルコ
スポラ・ロシコラなどのアブサイジン酸生産菌株
の培養物,培養液ならびにそれらの処理物などが
あげられる。セルコスポラ・ロシコラによるアブ
サイジン酸の生産については特開昭56−160996に
記載されている。尚、アブサイジン酸の構造式は
である。 Examples of solutions containing abscisic acid include cultures of abscisic acid-producing strains such as Cercospora rosicola, culture solutions, and processed products thereof. The production of abscisic acid by Cercospora rosicola is described in JP-A-160996. The structural formula of abscisic acid is It is.
強塩基性陰イオン交換樹脂としては、ダウエツ
クス1×2,同1×4,同1×8,同2×4,同
2×8(以上ダウケミカル社商品名,ダイヤイオ
ンSA10A,同SA11A,同SA21A,同PA316,同
PA408,同PA416,同HPA−10,同HPA−25
(以上三菱化成社商品名)、アンバーライト
IRA400,同IRA900,同IRA910(ロームアンドハ
ース社商品名)などが用いられる。 Strongly basic anion exchange resins include DOWEX 1x2, DOWEX 1x4, DOWEX 1x8, DOWEX 2x4, and DOWEX 2x8 (all Dow Chemical company product names, DOWEX SA10A, DIAION SA11A, DOWEX SA21A, PA316, same
PA408, PA416, HPA-10, HPA-25
(The above are Mitsubishi Kasei product names), Amberlight
IRA400, IRA900, IRA910 (Rohm and Haas product name), etc. are used.
ポリスチレン系多孔性吸着樹脂としては、ダイ
ヤイオンHP−10,同HP−20,同HP−30,同
HP−40,同HP50,同HP−21(以上三菱化成社
商品名)、アンバーライトXAD−2,同XAD−
4(ロームアンドハース社商品名)などが用いら
れる。 Diaion HP-10, Diamondion HP-20, Diamondion HP-30, Diamondion HP-30,
HP-40, HP50, HP-21 (all Mitsubishi Chemical product names), Amberlite XAD-2, XAD-
4 (Rohm and Haas Company product name), etc. are used.
強塩基性陰イオン交換樹脂を用いるときは、溶
出剤としては鉱酸(硫酸,塩酸など)、アルカリ
(可性ソーダ,可性カリ,アンモニアなど),塩類
(硫酸アンモニウム,硫酸ナトリウムなど)の水
溶液にメタノール,エタノール,プロパノール,
ブタノール,アセトンなどの水溶性有機溶媒を加
えた液が用いられる。添加する水溶性有機溶媒の
量が増えるに従つて、アブサイジン酸の溶出率は
高まる。有機溶媒の種類あるいはアブサイジン酸
の吸着量によつても左右されるが、水溶性有機溶
媒の使用範囲は30〜90%(v/v)が好適であ
る。 When using a strongly basic anion exchange resin, the eluent should be an aqueous solution of mineral acid (sulfuric acid, hydrochloric acid, etc.), alkali (potassible soda, potash, ammonia, etc.), or salt (ammonium sulfate, sodium sulfate, etc.). methanol, ethanol, propanol,
A solution containing a water-soluble organic solvent such as butanol or acetone is used. As the amount of water-soluble organic solvent added increases, the elution rate of abscisic acid increases. Although it depends on the type of organic solvent and the amount of abscisic acid adsorbed, the range of use of the water-soluble organic solvent is preferably 30 to 90% (v/v).
ポリスチレン系多孔性吸着樹脂を用いるときは
溶出液としては、該樹脂を使用する際に一般的に
用いられているメタノール,エタノール,プロパ
ノール,アセトンなどの有機溶媒を含む液を用い
る。 When using a polystyrene-based porous adsorption resin, a liquid containing an organic solvent such as methanol, ethanol, propanol, or acetone, which is commonly used when using the resin, is used as the eluent.
強塩基性陰イオン交換樹脂の場合に、鉱酸0.1
〜2N,アルカリ0.1〜2N,塩類0.1〜2Mなどの一
般的溶出剤を用いると、溶出されるアブサイジン
酸の量は10〜30%と回収率が低く実用的でない
が、水溶性有機溶媒を加えることによつて溶出率
を著しく高めることができる。 For strongly basic anion exchange resins, mineral acid 0.1
When using general eluents such as ~2N, alkali 0.1~2N, and salts 0.1~2M, the amount of abscisic acid eluted is 10~30%, which is low and impractical; however, adding a water-soluble organic solvent By this, the dissolution rate can be significantly increased.
ポリスチレン系多孔性吸着樹脂の場合には、上
記溶媒による溶出でほぼ100%に近い溶出率が得
られる。 In the case of polystyrene-based porous adsorption resin, an elution rate close to 100% can be obtained by elution with the above solvent.
アブサイジン酸を含む溶出液からのアブサイジ
ン酸の回収は以下のとおり行う。溶出液を減圧濃
縮し、有機溶媒を除去した後、PH2〜3に調整
し、酢酸エチル等の水に溶けにくい有機溶媒を加
えて抽出する。抽出液を分層後、無水硫酸ナトリ
ウムを加えて脱水し、必要があれば活性炭を加え
て脱色し、液を減圧濃縮し、アブサイジン酸を
結晶化させる。結晶分離後、真空乾燥して、アブ
サイジン酸の白色結晶を得ることができる。 Recovery of abscisic acid from the eluate containing abscisic acid is performed as follows. After the eluate is concentrated under reduced pressure to remove the organic solvent, the pH is adjusted to 2 to 3, and an organic solvent that is hardly soluble in water, such as ethyl acetate, is added for extraction. After separating the extract into layers, it is dehydrated by adding anhydrous sodium sulfate, and if necessary, activated carbon is added to decolorize it, and the liquid is concentrated under reduced pressure to crystallize abscisic acid. After crystal separation, white crystals of abscisic acid can be obtained by vacuum drying.
以下本発明の実施例を示す。 Examples of the present invention will be shown below.
実施例 1
100ml当り2.4gのポテトデキストロース・ブロ
ス(Difco社製品)と寒天2gを含む、ポテトデ
キストロース寒天培地(PH6.5)14mlを太型試験
管(160mm×16mm)に分注して120℃で15分間加圧
殺菌し、寒天斜面培地を調製した。寒天が凝固し
た後に寒天培地表面全域にセルコスポラ・ロシコ
ラIAM5031を接種して25℃で20日間静置培養し
た。得られた寒天斜面の培養物に8mlの殺菌水を
分注して、これにガラス棒を用いて菌体を懸濁
し、得られた懸濁液を種培養物とした。この種培
養物15mlをポテトデキストロース・ブロス
(Difco社製)2.4g/dl、ストツク(学名:
Mathiolaincana)の抽出物(花を刻み、同重量
の水を加えて、ホモゲナイズし、ガーゼで過し
た液)0.25ml/dl、PH6.5の発酵培地3を含
む5容ジヤーフアーメンターに接種し、1分間
当り3の空気を表面通気(0.10Kg moles/
hr)し、400rpmの撹拌条件下でかつ25℃の温度
条件下で培養し、培養5日目にノニオンOT221
(日本油脂社製品)を0.5mg/mlの濃度になるよう
添加して、培養を続け合計15日間培養を行なつ
た。培養液中にアブサイジン酸が50.5μg/ml蓄積
した。この培養液に過助剤ラジオライト#600
(昭和化学工業社製品)300gを加え、過を行な
い液を得た。この液をカラムに詰めたダイヤ
イオンSA21A(Cl)50mlに通塔し吸着させた後水
洗し、0.2N HCl−メタノール(1:1容量比)
溶液250mlでアブサイジン酸を溶出した。溶出液
を減圧濃縮した後酢酸エチル50mlを加えて、酢酸
エチル層にアブサイジン酸を抽出させた。酢酸エ
チル層を分層後、無水硫酸ナトリウム2gを加え
て脱水した後、硫酸ナトリウムを別し、液を
減圧濃縮し、アブサイジン酸を晶出させた。結晶
を分離後、室温にて真空乾燥しアブサイジン酸の
白色結晶110mgを得た。Example 1 Dispense 14 ml of potato dextrose agar medium (PH6.5) containing 2.4 g of potato dextrose broth (Difco product) and 2 g of agar per 100 ml into a wide test tube (160 mm x 16 mm) and heat at 120°C. The mixture was sterilized under pressure for 15 minutes to prepare an agar slant medium. After the agar had solidified, Cercospora rosicola IAM5031 was inoculated over the entire surface of the agar medium and cultured stationary at 25°C for 20 days. 8 ml of sterilized water was dispensed into the culture on the obtained agar slant, and the bacterial cells were suspended therein using a glass rod, and the resulting suspension was used as a seed culture. Add 15 ml of this seed culture to potato dextrose broth (manufactured by Difco) 2.4 g/dl, stock (scientific name:
Mathiolaincana) extract (chopped flowers, added the same weight of water, homogenized, and filtered through gauze) was inoculated into a 5-volume jar fermenter containing 0.25 ml/dl of fermentation medium 3 at pH 6.5. , surface ventilation of 3 air per minute (0.10Kg moles/
hr) and cultured under stirring conditions of 400 rpm and temperature conditions of 25°C, and on the 5th day of culture, nonionic OT221
(Nippon Oil & Fats Co., Ltd. product) was added at a concentration of 0.5 mg/ml, and the culture was continued for a total of 15 days. Abscisic acid accumulated in the culture solution at 50.5 μg/ml. Add radiolite #600 as a superfluid to this culture solution.
(Showa Chemical Industry Co., Ltd. product) 300g was added and filtered to obtain a liquid. This liquid was passed through 50 ml of Diaion SA21A (Cl) packed in a column to adsorb it, then washed with water, and 0.2N HCl-methanol (1:1 volume ratio)
Abscisic acid was eluted with 250 ml of solution. After the eluate was concentrated under reduced pressure, 50 ml of ethyl acetate was added to extract abscisic acid from the ethyl acetate layer. After separating the ethyl acetate layer, 2 g of anhydrous sodium sulfate was added for dehydration, the sodium sulfate was separated, and the liquid was concentrated under reduced pressure to crystallize abscisic acid. After separating the crystals, they were dried under vacuum at room temperature to obtain 110 mg of white crystals of abscisic acid.
実施例 2
実施例1と同様の方法で培養し63.2μg/mlの濃
度のアブサイジン酸を蓄積させた培養液2.6に
ラジオライト#600を300g加えて過し液を得
た。この液をカラムに詰めたアンバーライト
IRA400(OH)50mlに通塔した後、水洗を行なつ
た。つぎに2M NaCl−アセトン(6:4容量比)
溶液250mlでアブサイジン酸を溶出した。溶出液
を減圧濃縮した後、塩酸を加えてPH3に調整し、
酢酸エチル50mlを加えた。この後実施例1と同様
の方法で精製し、アブサイジン酸の白色結晶145
mgを得た。Example 2 300 g of Radiolite #600 was added to culture solution 2.6, which was cultured in the same manner as in Example 1 and accumulated abscisic acid at a concentration of 63.2 μg/ml, to obtain a filtrate. Amberlite packed with this liquid in a column
After passing through the column into 50 ml of IRA400 (OH), washing with water was performed. Next, 2M NaCl-acetone (6:4 volume ratio)
Abscisic acid was eluted with 250 ml of solution. After concentrating the eluate under reduced pressure, add hydrochloric acid to adjust the pH to 3.
50ml of ethyl acetate was added. After that, it was purified in the same manner as in Example 1, and white crystals of abscisic acid 145
I got mg.
実施例 3
実施例1と同様の方法で培養し57.6μg/mlの濃
度のアブサイジン酸を蓄積させた培養液2.6に
ラジオライト#600を300g加えて過し、液を
得た。この液をカラムに詰めたダイヤイオン
HP−20 50mlに通塔した後、0.2M NaClで洗浄
した。ついで30%アセトン水でアブサイジン酸を
溶出させた。溶出液を減圧濃縮した後、塩酸を加
えてPH2に調整し、酢酸エチルを50ml加えた。こ
の後実施例1と同様の方法で精製しアブサイジン
酸の白色結晶130mgを得た。Example 3 300 g of Radiolite #600 was added to culture solution 2.6, which was cultured in the same manner as in Example 1 and accumulated abscisic acid at a concentration of 57.6 μg/ml, and filtered to obtain a solution. Diaion packed with this liquid in a column
After passing through the column into 50 ml of HP-20, it was washed with 0.2M NaCl. Abscisic acid was then eluted with 30% acetone water. After the eluate was concentrated under reduced pressure, hydrochloric acid was added to adjust the pH to 2, and 50 ml of ethyl acetate was added. Thereafter, the product was purified in the same manner as in Example 1 to obtain 130 mg of white crystals of abscisic acid.
Claims (1)
む溶液をポリスチレン系多孔性吸着樹脂と接触さ
せることにより(+)シス−トランス型アブサイ
ジン酸を該樹脂に吸着させ、該物質を溶出剤で溶
出させるかまたは、(+)シス−トランス型アブ
サイジン酸を含む溶液を強塩基性陰イオン交換樹
脂と接触させることにより(+)シス−トランス
型アブサイジン酸を該樹脂に吸着させ、メタノー
ル、エタノール、プロパノール、ブタノールおよ
びアセトンから選ばれる水溶性有機溶媒を含む溶
出剤を用いて該物質を溶出させることを特徴とす
る(+)シス−トランス型アブサイジン酸の精製
法。 2 有機溶媒が30〜90%(v/v)含まれる溶出
剤を用いることを特徴とする特許請求の範囲第1
項記載の方法。[Claims] 1. By contacting a solution containing (+) cis-trans abscisic acid with a polystyrene-based porous adsorption resin, the (+) cis-trans abscisic acid is adsorbed onto the resin, and the substance is Either by elution with an eluent or by contacting a solution containing (+) cis-trans abscisic acid with a strongly basic anion exchange resin, (+) cis-trans abscisic acid is adsorbed onto the resin, and methanol A method for purifying (+) cis-trans type abscisic acid, which comprises eluting the substance using an eluent containing a water-soluble organic solvent selected from , ethanol, propanol, butanol, and acetone. 2. Claim 1, characterized in that an eluent containing 30 to 90% (v/v) of an organic solvent is used.
The method described in section.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19267482A JPS5982340A (en) | 1982-11-02 | 1982-11-02 | Purification of abscisic acid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19267482A JPS5982340A (en) | 1982-11-02 | 1982-11-02 | Purification of abscisic acid |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5982340A JPS5982340A (en) | 1984-05-12 |
JPH036139B2 true JPH036139B2 (en) | 1991-01-29 |
Family
ID=16295150
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP19267482A Granted JPS5982340A (en) | 1982-11-02 | 1982-11-02 | Purification of abscisic acid |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5982340A (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04202176A (en) * | 1990-11-29 | 1992-07-22 | Toray Ind Inc | Purification of abscisic acid |
CN1306035C (en) * | 2004-09-14 | 2007-03-21 | 中国科学院成都生物研究所 | Method for extracting natural abscisic acid |
JP2007222203A (en) * | 2006-02-21 | 2007-09-06 | Sumida Corporation | Mirror driving mechanism and imaging device equipped with mirror driving mechanism |
CN116730831B (en) * | 2023-07-03 | 2024-04-12 | 江西新瑞丰生化股份有限公司 | Extraction method of abscisic acid mother liquor |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56160996A (en) * | 1980-05-15 | 1981-12-11 | Kyowa Hakko Kogyo Co Ltd | Preparation of abscisic acid by fermentation method |
-
1982
- 1982-11-02 JP JP19267482A patent/JPS5982340A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56160996A (en) * | 1980-05-15 | 1981-12-11 | Kyowa Hakko Kogyo Co Ltd | Preparation of abscisic acid by fermentation method |
Also Published As
Publication number | Publication date |
---|---|
JPS5982340A (en) | 1984-05-12 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4861870A (en) | Process for purifying anthracyclinone glycosides by selective adsorption on resins | |
SK832006A3 (en) | A method for polymyxin B isolation from fermented soil. | |
EP2402306B1 (en) | Method for producing 5-aminolevulinic acid hydrochloride | |
US5986089A (en) | Process for the preparation of moenomycin A | |
JPH036139B2 (en) | ||
JP2001258583A (en) | Method for purifying shikimic acid | |
JP3421338B2 (en) | Method for producing vancomycin | |
US5258495A (en) | Process for making vancomycin HC1 | |
GB2085884A (en) | Crystals of beta -nicotinamide- adenine-dinucleotide and process for preparing the same | |
US5180670A (en) | Method for purification of mitomycin C | |
JP3382297B2 (en) | Method for producing high purity deferoxamine salt | |
JPH07165702A (en) | Method for isolating natural type abscisic acid | |
JP2971128B2 (en) | Purification method of mitomycin C | |
CN113511967B (en) | Method for extracting quinic acid from ginkgo leaf extract chromatographic wastewater | |
US5026640A (en) | Process for the conversion of corrinoids produced by microorganisms into cyanocorrinoids | |
JPS6337635B2 (en) | ||
EP0009363A1 (en) | Method of separating cephalosporins | |
JPH04202176A (en) | Purification of abscisic acid | |
JPS6216497A (en) | Purification of cytidine-5'-diphosphate choline | |
RU1822885C (en) | Method of isolation of 4- and/or 5-hydroxyindolyl-3-acetic acids | |
KR840002477B1 (en) | Method of separating cephalosporing | |
US2677644A (en) | Purification of vitamin b12 solutions | |
JPS62293A (en) | Production of l-rhamnose | |
JPH0776570A (en) | Isolation of abscisic acid | |
GB2180538A (en) | Process for the separation of corrinoids |