JPS5982340A - Purification of abscisic acid - Google Patents

Purification of abscisic acid

Info

Publication number
JPS5982340A
JPS5982340A JP19267482A JP19267482A JPS5982340A JP S5982340 A JPS5982340 A JP S5982340A JP 19267482 A JP19267482 A JP 19267482A JP 19267482 A JP19267482 A JP 19267482A JP S5982340 A JPS5982340 A JP S5982340A
Authority
JP
Japan
Prior art keywords
acid
abscisic acid
resin
cis
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.)
Granted
Application number
JP19267482A
Other languages
Japanese (ja)
Other versions
JPH036139B2 (en
Inventor
Shinzo Ishii
石井 真三
Takemitsu Arai
新井 雄光
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
KH Neochem Co Ltd
Original Assignee
Kyowa Hakko Kogyo Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Kyowa Hakko Kogyo Co Ltd filed Critical Kyowa Hakko Kogyo Co Ltd
Priority to JP19267482A priority Critical patent/JPS5982340A/en
Publication of JPS5982340A publication Critical patent/JPS5982340A/en
Publication of JPH036139B2 publication Critical patent/JPH036139B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To obtain the titled acid useful as a natural-type plant hormone from a solution containing (+)-cis-trans abscisic acid, in high yield, by using a strongly basic anion exchange resin of a polystyrene-type porous adsorbent resin as an adsorbent. CONSTITUTION:A solution containing (+)-cis-trans abscisic acid such as the cultured product of an abscisic acid-producing strain (e.g., Cercospora rosicola), its cultured liquid, or their treated material, is made to contact with a strongly basic anion exchange resin or a polystyrene-type porous adsorbent resin to effect the adsorption of the abscisic acid to the resin. The adsorbed acid is eluted with an elutant containing 30-90%(v/v) of an organic solvent selected preferably from methanol, ethanol, propanol, butanol and acetone. Abscisic acid in the above solution can be purified economically, in an industrial scale by this process.

Description

【発明の詳細な説明】 本発明は(ト)シスートランス型アブサイジ/酸(以下
アブサイシン酸と略記する)の精ネー法に関する。さら
に詳細には、本発明d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(ト)シス−ト
ランス型アブブ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 refining (t)cis-trans abscisic acid (hereinafter abbreviated as abscisic acid). More specifically, the present invention d relates to a method for purifying (t)cis-trans type abbuidic acid using a strongly basic anion exchange resin or a polystyrene-based porous adsorption resin.

アブサイシ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。
Absaicic 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シン酸の生成につイテハ、セ
ルコスホ2・ロシコラ(1’1rcosρra rpz
i■h)による固体培会および液体静置光照射培会が知
られているが、アブサイシン酸の生成景ハ少なく培養期
間は30〜40日の長期を要し、工業的には難点があっ
た。また培養物・培養液からアブサイシン酸を精製単離
する方法としては、。
Regarding the production of abscisic acid by conventional fermentation method,
A solid culture medium and a liquid stationary light irradiation culture according to i. Ta. In addition, as a method for purifying and isolating abscisic acid from culture materials and broth,

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(C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、工桑的にはやはり作意があっ
た。(Experientia 3315561977
年)。
A known method is to add an organic solvent that is hardly soluble in water, such as ethyl acetate, and extract the organic solvent layer (C) for purification, but since a large amount of organic solvent is used, this method was inconvenient. (Experientia 3315561977
Year).

最近上述のセルコスポラ・ロシコラによる通気攪拌液体
深部培養が見出され、培養期間15〜20日で培養液中
にアブサイシン酸が60μ97M以上蓄積することが明
らかにされ、工業化が可能となった。また培養液からの
アブサイシン酸の精製単離は従来知られていた溶媒抽庄
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
ことが明らかとなった(特開昭56−160996)。
Recently, the above-mentioned submerged aerated liquid culture of Cercospora rosicola was discovered, and it was revealed that more than 60μ97M of abscisic acid was accumulated in the culture solution within a culture period of 15 to 20 days, making industrialization possible. It has also been revealed 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 conventional solvent extraction (Japanese Patent 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柩めて収率が悪い欠点が
あった。
However, solvent extraction has the disadvantage of using a large amount of solvent, and conventional methods using ion exchange resins have the drawback of generally poor yields.

そこで本発明者らは、培養液からアブサイシン酸を工業
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
樹脂にアブサイシン酸を含む培養炉液を接触させること
により、これらの樹脂にアブサイシン酸を吸着さぜ、強
塩基性陰イオン交換樹脂に吸催したアブサイシン酸はメ
タノール、アセトン等の水溶性有機溶媒を含んだ酸″!
r、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シン酸は該樹脂を使
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った。
Therefore, the present inventors investigated various methods for purifying abscisic acid from a culture solution on an industrial scale. As a result, by bringing the culture solution containing abssaic acid into contact with a strongly basic anion exchange resin or polystyrene-based porous adsorption resin, abssaic acid is adsorbed onto these resins and absorbed into the strongly basic anion exchange resin. Absaicic acid is an acid containing water-soluble organic solvents such as methanol and acetone!
The present invention was accomplished by discovering that absisic acid adsorbed to a porous polystyrene adsorption resin can be recovered in good yield by a common eluent used when using such resins. reached.

従来、アブサイシ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剤を含むもの
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ったく知られていない。
Conventionally, methods using these strongly basic anion exchange resins have been known for the purification of absisic acid [Japanese Unexamined Patent Application Publication No. 1983-1993]
-160996] It is not known that the elution rate can be significantly increased by using an eluent containing a water-soluble organic solvent, and furthermore, there is no known example of using a polystyrene-based porous adsorption resin. .

以下本発明の詳細な説明するっ 本発明によれば、アブサイシ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成N樹脂
と接触させることにより、アブサイシン酸を該樹脂に吸
着させ、しかる後に溶出剤により溶出することによりア
ブサイシン酸を精製することができる。・ アブサイシン酸を含む溶液は、たとえばセルコスポラ・
ロシコラなどのアブサイシン貢生産菌株の培發物、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レン酸の生産については
特ビi昭56−160996に記載されている。
The present invention will be described in detail below.According to the present invention, by contacting a solution containing abssaicic acid with a strongly basic anion exchange resin or a polystyrene-based porous N resin, abssaicic acid is adsorbed onto the resin. , followed by elution with an eluent to purify absisic acid.・Solutions containing abscisic acid can be used to treat, for example, Cercospora
Examples include culture products, culture fluids, and processed products of abscisin-producing strains such as Rosicola. The production of absilic acid by Cercospora rosicola is described in Japanese Patent Publication No. 56-160996.

強塩基性陰イオン交換樹脂としては、ダウエックス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5AIOA、同5A
IIA、同S A21A。
As a strong basic anion exchange resin, DOWEX 1x
2. Same 1×4. Same 1×8. Same 2 x 4゜ Same 2 x 8 (The above are Dow Chemical Company product names, Diamond 5AIOA, 5A
IIA, S A21A.

同PA316.同PA406.同PA4i6゜同5AI
IA、同HPA−25(以上三菱化成社商品名)、アン
バーライ)IRA4°0゜同IRA900.同IRA9
10(ロー、ヘアンドハース社商品名)などが用いられ
る。
Same PA316. Same PA406. Same PA4i6゜ Same 5AI
IA, HPA-25 (all Mitsubishi Kasei product names), Amberly) IRA4°0° IRA900. Same IRA9
10 (Low, trade name of Herr & Haas), 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I(P−20,同HP−30.同HP−
40.同HP−50,同HP−21(以上三菱化成社商
品名)、アンノく−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。
As the polystyrene-based porous adsorption resin, Diamondion HP-10, Diamondion I (P-20, Diamondion HP-30, Diamondion HP-
40. HP-50, HP-21 (all Mitsubishi Kasei product names), Annoku Light XAD-2, XAD-4 (
Rohm and Haas product name) etc. are used.

強塩基性陰イオン交換樹脂を用いるときは、1ぬ芝==
コ=フ溶出剤としては鉱酸(硫酸。
When using a strong basic anion exchange resin,
A mineral acid (sulfuric acid) is used as a CO-F eluent.

塩酸など)、アルカリ(再往ソーダ、再往力1ハアンモ
ニアなど)、塩類(硫酸アンモニウム。
Hydrochloric acid, etc.), alkalis (sodium chloride, ammonia, etc.), salts (ammonium sulfate, etc.).

硫酸ナトリウムなど)の水溶液にメタノール。methanol to an aqueous solution of sodium sulfate, etc.).

エタノール、グロパノール、ブタノール、アセト/など
の水溶性有機溶媒を加えだ液が用いられる。添加する水
溶性有機溶剤の量が増えるに従って、アブサイシン酸の
溶出率は高まる。
A solution prepared by adding a water-soluble organic solvent such as ethanol, gropanol, butanol, or acetate is used. As the amount of water-soluble organic solvent added increases, the elution rate of absisic acid increases.

有伝浴媒の種類あるいはアブサイシン酸の吸着量によっ
ても左右されるが、水溶性有機溶媒の使用範囲は30〜
90係(v/v )が好適である。
Although it depends on the type of bath medium and the amount of absisic acid adsorbed, the usage range of water-soluble organic solvents is 30~
90 ratio (v/v) is suitable.

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。
When using a polystyrene-based porous adsorption resin, the eluent may be methanol or ethanol, which are commonly used when using the resin.

グロバノール、アセトンなどの有機溶媒を含む液を用い
る。
A liquid containing an organic solvent such as globanol or acetone is used.

強塩基性陰イオン交換樹脂の場合に、鉱酸0.1〜2 
N 、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シン酸の
量は10〜30チ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って溶出率を著しく高める
ことができる。
In the case of strongly basic anion exchange resin, mineral acid 0.1-2
When general eluents such as N, alkali 0.1-2N, and salts 0.1-2M are used, the amount of abscisic acid eluted is 10-30%, which is a low recovery rate and is not practical. The dissolution rate can be significantly increased by adding a solvent.

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 a polystyrene-based porous adsorption resin, an elution rate close to 100% can be obtained by elution with the above solvent.

アブサイシン酸を含む溶出液からのアブサイシン酸の回
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、p’f(2〜3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、涙液を減圧濃縮し、アブサ
イシン酸を結晶化させる。結晶分離後、真空乾燥して、
アブサイシン酸の白色結晶を得ることができる。
Absaicic acid is recovered from the eluate containing abssaicic acid as follows. After concentrating the eluate under reduced pressure and removing the organic solvent, the p'f (adjusted to 2 to 3) is extracted by adding an organic solvent that is hardly soluble in water such as ethyl acetate. After separating the extract into layers, add anhydrous sulfuric acid. Dehydrate by adding sodium, decolorize by adding activated carbon if necessary, concentrate the tear fluid under reduced pressure, and crystallize absisic acid.After crystal separation, vacuum dry.
White crystals of abscisic acid can be obtained.

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゜ i00+xA!当す2.4 pのポテトデキストロース
・プロス(Difco社製品)と寒天22を含む、ポテ
トデキストロース寒天培地(PH6、s)x4m#を大
型試験管(160xn x 16 m)に分注して12
0℃で15分間加圧殺菌し、寒天斜面培地を調製した。
Example 1゜i00+xA! Dispense 4 m # of potato dextrose agar medium (PH6, s) containing 2.4 p of potato dextrose prosthe (product of Difco) and 22 m of agar into large test tubes (160 x n x 16 m).
The mixture was sterilized under pressure at 0°C for 15 minutes to prepare an agar slant medium.

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。倚られた寒天斜面の培養物に8ゴの殺菌水
を分注して、これにガラス棒を用いて函体を懸濁し、得
られた懸濁液を種培養物とした。この桔培養物15m1
をポテトデキストロース・ブロス(Difco社製) 
2.497d!、ストック(学名:庵thiolain
ca部)の抽出物(花を刻み、同重量の水を加えて、ホ
モゲナイズし、ガーゼで流過し戸:涙液)0.25罰/
L:tl、pH6,5の発酵培地31を含む51容ジャ
ーファーメンタ−に接種し、1分間pす3Aの空気を表
面通気(0,10匂rnolea/y&hr) L、4
0Orpmの攪拌条件下でかつ25℃の温度条件下で培
養し、培養5日月にノニオン0T221(日本油脂社製
品)を0.5 m9 / mJの濃度に々るよう添加し
て、培養を続は合計J5日間培養を行なった。培養液中
にアブサイシン酸が50.5μ7Δa蓄積した。この培
養液に濾過助剤ラジオライ+1600 (昭和化学工条
社製品)300f加え、漣過を行ない涙液を得だ。この
涙液をカラムに詰めたダイヤイオンS A21 A (
Cl)50ゴに通塔し吸着さぜた後水洗し、0.2 N
 Hα−メタノール(1:1容量比)溶液250ゴでア
ブサイシン酸を溶出した。溶出液を減圧濃縮した後酢酸
エチル50vclを加えて、酢酸エチル層にアブサイシ
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、硫酸ナトリウムを沢
別し、涙液を減圧濃縮し、アブサイシン酸を晶出させた
。結晶を分離後、室温にて真空乾燥しアブサイシン酸の
白色結晶1107717を得た。
After the agar solidifies, Cercospora spp.
Rosicola IAM5031 was inoculated and statically cultured at 25°C for 20 days. Eight gallons of sterilized water was dispensed onto the culture on the crushed agar slant, and the box was suspended in this using a glass rod, and the resulting suspension was used as a seed culture. 15ml of this persimmon culture
Potato dextrose broth (manufactured by Difco)
2.497d! , stock (scientific name: hermitage thiolain)
ca part) extract (chop the flowers, add the same weight of water, homogenize, and drain through gauze: lachrymal fluid) 0.25 punishment/
L: Inoculate a 51-volume jar fermenter containing fermentation medium 31 with tl, pH 6.5 and incubate for 1 minute with 3 A of air aerated on the surface (0.10 odor nolea/y & hr) L, 4
The cells were cultured under agitation conditions of 0 rpm and a temperature of 25°C, and nonionic 0T221 (product of NOF Co., Ltd.) was added to a concentration of 0.5 m9/mJ for 5 days after culture, and the culture was continued. The cells were cultured for a total of J5 days. 50.5μ7Δa of abscisic acid was accumulated in the culture solution. To this culture solution, 300 f of a filter aid Radioly+1600 (manufactured by Showa Kagaku Kojosha) was added and filtrated to obtain lachrymal fluid. Diaion S A21 A (
Cl) was passed through a column of 50 g to adsorb it, washed with water, and diluted with 0.2 N
Absaicic acid was eluted with 250 g of Hα-methanol (1:1 volume ratio) solution. After the eluate was concentrated under reduced pressure, 50 vcl of ethyl acetate was added to extract absisic 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 removed, and the lachrymal fluid was concentrated under reduced pressure to crystallize absisic acid. After separating the crystals, they were vacuum dried at room temperature to obtain white crystals of abscisic acid 1107717.

実施例2゜ 実施例1と同様の方法で培養し63.2μ?/rdの濃
度のアブサイシン酸を蓄積させた培養液2.61にラジ
オライト+600を300f加えて済過し涙液を得た。
Example 2: Cultured in the same manner as in Example 1, 63.2μ? A tear fluid was obtained by adding 300f of Radiolite+600 to 2.61ml of a culture solution in which abscisic acid had been accumulated at a concentration of /rd.

このろ液をカラムに詰めたアンバーライトIR人400
 (OI() 50 vtlに通塔した後、水洗を行な
った。つぎに2M NaCA! −アセトン(6:4容
量比)溶液250IILlでアブサイシン酸を溶出した
。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50−を加えた。この後実施例1と同様
の方法で精製し、アブサイシン酸の白色結晶145■を
得た。
Amberlite IR person 400 filled with this filtrate in a column
(OI()) After passing through the column to 50 vtl, washing with water was performed. Absaicic acid was then eluted with 250 IIL of a 2M NaCA!-acetone (6:4 volume ratio) solution. After concentrating the eluate under reduced pressure, hydrochloric acid was removed. In addition, the pH was adjusted to 3, and 50 cm of ethyl acetate was added thereto.After that, the mixture was purified in the same manner as in Example 1 to obtain 145 cm of white crystals of absisic acid.

実施例3゜ 実施例1と同様の方法で培養し57.6μg′〜の濃度
のアブサイシン酸を蓄積させた培養液2.61にラジオ
ライトf 600を300?加えて済過し、涙液を得た
。この涙液をカラムに詰めだダイヤイオンI(P −2
050mgに通塔した後、0.2MNaC1で洗浄した
。ついで30%アセトン水でアブサイシン酸を溶出させ
た。溶出液を減圧a縮した後、塩酸を加えてpH2に調
整し、酢酸エチルを50ゴ加えた。この後実施例1と同
様の方法で精製しアブサイシン酸の白色結晶1、30 
mpを得り。
Example 3: Radiolite f 600 was added to 2.61 μg of a culture solution cultured in the same manner as in Example 1 to accumulate abscisic acid at a concentration of 57.6 μg' to 300 μg. In addition, the patient passed away and obtained lachrymal fluid. This tear fluid was packed into a column called Diamond Ion I (P-2).
After passing through the column to 0.050 mg, it was washed with 0.2M NaCl. Absaicic acid was then eluted with 30% acetone water. After condensing the eluate under reduced pressure, hydrochloric acid was added to adjust the pH to 2, and 50 g of ethyl acetate was added. Thereafter, it was purified in the same manner as in Example 1, and white crystals of abscisic acid 1,30
Get mp.

特許出願人(lo2)協和醗酵工業株式会社71 手続補正書 昭和57年12月28日 特許庁長官 殿 1、事件の表示 昭和57年特許願第 /9267り号 2発明の名称 アブサイシン酸のffff法 3、補正をする者 事件との関係 特許出願人 郵便査号 100 住 所 東京都千代田区大手町−丁目6 着1号名称 
<102)  協和醗酵工業株式会社(T五r−: 0
3−201−7211内線2751)明細書の特許請求
の範囲の植j lr! 特許請求の範囲 (11←〕フシスートランスアブサイシン酸を含む溶液
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し←)シス−トランス
型アブサイシン酸を該樹脂に吸着させ、該物質を溶出剤
で溶出することを特徴とする←)シス−トランス型アブ
サイシン酸の精製法。
Patent Applicant (LO2) Kyowa Hakko Kogyo Co., Ltd. 71 Procedural Amendment December 28, 1980 Commissioner of the Patent Office 1. Indication of the Case 1988 Patent Application No./9267 No. 2 Name of the Invention ffff method of absisic acid 3. Relationship with the case of the person making the amendment Patent applicant Postal code 100 Address 6 Otemachi-chome, Chiyoda-ku, Tokyo Address No. 1 Name
<102) Kyowa Hakko Kogyo Co., Ltd. (T5r-: 0
3-201-7211 extension 2751) Inscription of claims in the specification j lr! Claims (11←) By contacting a solution containing cis-trans-absaicic acid with a strongly basic anion exchange resin or a polystyrene-based porous adsorption resin←) cis-trans-absaicic acid is added to the resin. ←) A method for purifying cis-trans abscisic acid, which comprises adsorbing the substance and eluting the substance with an eluent.

(2)強塩基性陰イオン交換樹脂を用いる場合、溶出剤
が有機溶媒を含むことを特徴とする特許請求の範囲第1
項記載の方法。
(2) When using a strongly basic anion exchange resin, the eluent contains an organic solvent.
The method described in section.

(3)有機溶媒゛がメタノール、エタノール、グロバノ
ール、ブタノールおよびアセトンから選ばれることを特
徴とする特許請求の範囲第2項記載の方法。
(3) A method according to claim 2, characterized in that the organic solvent is selected from methanol, ethanol, globanol, butanol and acetone.

(4)有機溶媒が30〜90%(v/v)含まれること
を特徴とする特許請求の範囲第2または3項の方法。
(4) The method according to claim 2 or 3, characterized in that the organic solvent is contained in an amount of 30 to 90% (v/v).

Claims (4)

【特許請求の範囲】[Claims] (1)(ト)シス−トランス型アブサイシン酸を含む溶
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
孔性吸着樹脂と接融させることにより(ト)シス−;・
ランス型アブサイシン酸を該樹脂に吸着させ、該物質を
溶出剤で溶出することを特徴とする(ト)シス−トラン
ス型アブサイシン酸の精製法。
(1) By melting a solution containing (g) cis-trans abscisic acid with a strongly basic anion exchange resin or a porous polystyrene adsorption resin, (g) cis-;・
1. A method for purifying (t)cis-trans type abscisic acid, which comprises adsorbing lance type abscisic acid on the resin and eluting the substance with an eluent.
(2)溶出剤が有機溶媒を含むことを特徴とする特許請
求の範囲第1項記載の方法。
(2) The method according to claim 1, wherein the eluent contains an organic solvent.
(3)有機溶媒がメタノール、エタノール、プロパンー
ル、ブタ/−ルおよびアセトンから選ばれるととを特徴
とする特許請求の範囲第2項記載の方法。
3. A method according to claim 2, characterized in that the organic solvent is selected from methanol, ethanol, propanol, butyl and acetone.
(4)有機溶媒が30〜90 % (v/v)含まれる
ことを特徴とする特許請求の範囲第2または3項の方法
(4) The method according to claim 2 or 3, characterized in that the organic solvent is contained in an amount of 30 to 90% (v/v).
JP19267482A 1982-11-02 1982-11-02 Purification of abscisic acid Granted JPS5982340A (en)

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 true JPS5982340A (en) 1984-05-12
JPH036139B2 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)

Cited By (4)

* Cited by examiner, † Cited by third party
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
CN116730831A (en) * 2023-07-03 2023-09-12 江西新瑞丰生化股份有限公司 Extraction method of abscisic acid mother liquor

Citations (1)

* Cited by examiner, † Cited by third party
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

Patent Citations (1)

* Cited by examiner, † Cited by third party
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

Cited By (5)

* Cited by examiner, † Cited by third party
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
CN116730831A (en) * 2023-07-03 2023-09-12 江西新瑞丰生化股份有限公司 Extraction method of abscisic acid mother liquor
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

Also Published As

Publication number Publication date
JPH036139B2 (en) 1991-01-29

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