JPS62126185A - Production of isoflavone derivative - Google Patents

Production of isoflavone derivative

Info

Publication number
JPS62126185A
JPS62126185A JP26612485A JP26612485A JPS62126185A JP S62126185 A JPS62126185 A JP S62126185A JP 26612485 A JP26612485 A JP 26612485A JP 26612485 A JP26612485 A JP 26612485A JP S62126185 A JPS62126185 A JP S62126185A
Authority
JP
Japan
Prior art keywords
solvent
organic solvent
pueraria
root
water
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
JP26612485A
Other languages
Japanese (ja)
Other versions
JPH0421669B2 (en
Inventor
Takuo Kosuge
小菅 卓夫
Kinji Ishida
均司 石田
Zenzo Kitada
北田 善三
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.)
Tsumura and Co
Original Assignee
Tsumura Juntendo Inc
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 Tsumura Juntendo Inc filed Critical Tsumura Juntendo Inc
Priority to JP26612485A priority Critical patent/JPS62126185A/en
Publication of JPS62126185A publication Critical patent/JPS62126185A/en
Publication of JPH0421669B2 publication Critical patent/JPH0421669B2/ja
Granted legal-status Critical Current

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  • Saccharide Compounds (AREA)
  • Pyrane Compounds (AREA)

Abstract

PURPOSE:To industrially and advantageously obtain the titled compound useful for a medicament, by bringing an extract solution of pueraria root as it is or after distilling a solvent off, into contact with a synthetic adsorbent resin to adsorb an isoflavone derivative, followed by elution thereof by using such as an organic solvent. CONSTITUTION:An extract solution of pueraria root (root of Pueraria Iobata Ohwi, etc. are preferred), as it is or after distilling a solvent off, preferably after adjusting its pH at 5.5-7.0, is brought into contact with a synthetic adsorbent resin (example; styrene-divinylbenzene polymeric resin, etc.) to adsorb an isoblavone derivative expressed by the formula. The the compound is eluted with an organic solvent (preferably methanol) or a mixed solvent of the organic solvent with water to obtain the aimed compound. By utilizing the extract solution of the pueraria root produced in production of pueraria starch, it can be produced at a lower cost.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、簡便かつ安価な、イソフラボン誘導体の製造
方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a simple and inexpensive method for producing isoflavone derivatives.

[従来の技術および問題点] マメ科(Leguminosae)の葛の根は葛根と呼
ばれ、古来より和漢薬として漢方処方に用いられてきた
[Prior Art and Problems] Kudzu root, which belongs to the leguminosae family, is called kudzu root and has been used in Chinese medicine as a Japanese and Chinese medicine since ancient times.

この葛根には下記式 で表されるプエラリン、ダイズイン、ダイゼイン等のイ
ソフラボン誘導体が含まれており、ダイゼインのマウス
摘出小腸におけるパパベリン様鎮痙作用[薬学雑誌、9
7,103(1977)]をはじめとして多くの薬理作
用が知られている。従って、今後これらのイソフラボン
誘導体を医薬品として提供する場合、いかに安価に、か
つ大量にイソフラボン誘導体を得るかが重要な因子とな
る。
This arrowroot contains isoflavone derivatives such as puerarin, daidzein, and daidzein expressed by the following formula, and daidzein has a papaverine-like antispasmodic effect in the isolated small intestine of mice [Pharmaceutical Journal, 9
7, 103 (1977)], many pharmacological actions are known. Therefore, if these isoflavone derivatives are to be provided as pharmaceuticals in the future, how to obtain them cheaply and in large quantities will be an important factor.

従来、イソフラボン誘導体を得るには、葛根の有機溶媒
または、含水有機溶媒による抽出液をアルミナ、シリカ
ゲル等を吸着剤とするカラムクロマトグラフィーで精製
する方法がとられていた。
Conventionally, isoflavone derivatives have been obtained by purifying an extract of arrowroot with an organic solvent or a water-containing organic solvent by column chromatography using alumina, silica gel, or the like as an adsorbent.

また、葛根の極性溶媒抽出液またはM澱粉製造時の廃液
に酢酸鉛を加えて析出する沈殿を除去し、シ戸液にアン
モニアを添加し、中性ないし弱塩基性にすることにより
生成する沈殿を、硫化水素で処理して有効成分を得る方
法ら知られている。
In addition, lead acetate is added to the polar solvent extract of arrowroot or the waste liquid from M starch production to remove the precipitate, and ammonia is added to the Shito liquid to make it neutral or weakly basic. A known method is to obtain the active ingredient by treating with hydrogen sulfide.

しかし、これらの方法を工業的大量精製に適用する場合
、吸着剤への負荷量が顕著に多くなることや、規模拡大
のために操作が煩雑になる等の不都合が生じろため、得
られるイソフラボン誘導体は少量でしかも高価なものに
な・る。また、イソフラボン誘導体の工業的な精製はほ
とんど行なイっれていない。
However, when these methods are applied to industrial large-scale purification, there are disadvantages such as a significant increase in the amount of loading on the adsorbent and complicated operations due to scale expansion. Derivatives are available in small quantities and are expensive. Furthermore, industrial purification of isoflavone derivatives has hardly been carried out.

[問題点を解決するための手段] 本発明者等は、安価に、かつ大量にイソフラボン誘導体
を得るための方法について鋭意検討した結果、葛根の抽
出液をそのままらしくは溶媒を留去して合成吸着樹脂に
接触させて、イソフラボン誘導体を吸着せしめ、次いで
有機溶媒または有機溶媒と水との混合溶媒を用いて該合
成樹脂から溶出さU“ることにより安価に、かつ大量に
イソフラボン誘導体が得られることを見出し、本発明を
完成させた。
[Means for Solving the Problems] As a result of intensive study on a method for obtaining isoflavone derivatives at low cost and in large quantities, the present inventors have synthesized the extract by distilling off the solvent from the extract of arrowroot. Isoflavone derivatives can be obtained inexpensively and in large amounts by contacting with an adsorption resin to adsorb the isoflavone derivatives, and then eluting them from the synthetic resin using an organic solvent or a mixed solvent of an organic solvent and water. They discovered this and completed the present invention.

以下に本発明の詳細な説明する。The present invention will be explained in detail below.

葛根の抽出液を得る際に、抽出に用いられる葛根は、菌
属(Puerariae属)の根、更に好ましくは、P
ueraria Iobata Ohwi (Puer
aria pseudo−hirsuta Tang 
et fang)またはPueraria Iobat
aOhwi var、 chinensis (Ben
th) Ohwi(Leguminosae)の根を用
いることができる。抽出溶媒は水、メタノール、エタノ
ール等の水性溶媒または水と水性溶媒との混合溶媒が挙
げられ、室温から抽出溶媒の沸点までの温度範囲内で抽
出する。
When obtaining an extract of arrowroot, the arrowroot used for extraction is a root of the genus Puerariae, more preferably a root of the genus Puerariae.
uelaria Iobata Ohwi (Puer
aria pseudo-hirsuta Tang
et fang) or Pueraria Iobat
aOhwi var, chinensis (Ben
th) The root of Ohwi (Leguminosae) can be used. Examples of the extraction solvent include water, an aqueous solvent such as methanol, and ethanol, or a mixed solvent of water and an aqueous solvent, and extraction is performed within a temperature range from room temperature to the boiling point of the extraction solvent.

また、現在、葛澱粉の製造は葛根を水抽出し、抽出液中
に沈殿した水不溶性澱粉を取ることにより行われており
、この際葛根の抽出液は廃液として捨てられているが、
本発明で言うところの葛根の抽出液は、このような廃液
をも包含する。従って、従来全く利用されていなかった
葛澱粉製造時の葛根の抽出液を利用すれば、より安価に
イソフラボン誘導体を得ることができる。
Currently, arrowroot starch is produced by extracting arrowroot with water and removing the water-insoluble starch precipitated in the extract.At this time, the arrowroot extract is discarded as waste liquid.
The extract of arrowroot as referred to in the present invention also includes such waste liquid. Therefore, isoflavone derivatives can be obtained at lower cost by using the extract of arrowroot root used in the production of arrowroot starch, which has not been used at all in the past.

次に、前記抽出液をそのままもしくは溶媒を留去して合
成吸着樹脂に接触させて、イソフラボン誘導体を吸着せ
しめる。抽出液に酸性度、塩基仕度の違いがある場合は
、イソフラボン誘導体の合成吸着樹脂への吸着率を向上
させるために適宜、適当な酸やアルカリを添加してp1
15.5〜pl+7.0程度の条件に保つのが望ましく
、この際の酸としては酢酸、塩酸等が挙げられ、アルカ
リとしては炭酸水素ナトリウム、水酸化ナトリウム等が
挙げられる。
Next, the extract is brought into contact with a synthetic adsorption resin, either as it is or after the solvent is distilled off, to adsorb isoflavone derivatives. If the extract has a difference in acidity or basicity, add an appropriate acid or alkali as needed to improve the adsorption rate of isoflavone derivatives to the synthetic adsorption resin.
It is desirable to maintain the condition at about 15.5 to pl+7.0, and examples of the acid in this case include acetic acid, hydrochloric acid, etc., and examples of the alkali include sodium hydrogen carbonate, sodium hydroxide, etc.

また、前記抽出時に抽出溶媒として水性溶媒を使用して
いる場合は、イソフラボン誘導体の合成吸着樹脂への吸
着率を向上させるために、抽出液から使用した水性溶媒
を留去しておくことが望ましい。
In addition, if an aqueous solvent is used as the extraction solvent during the extraction, it is desirable to distill off the used aqueous solvent from the extract in order to improve the adsorption rate of isoflavone derivatives to the synthetic adsorption resin. .

合成吸着樹脂の具体例としては、「ダイヤイオンHP樹
脂」(三菱化成工業昧式会社製)、「アンバーライトX
AD樹脂」(ロームアンドハース株式会社製)、「デュ
オライトS樹脂」(ダイヤモンドシャムロツタ社製)等
が挙げられる。
Specific examples of synthetic adsorption resins include “Diaion HP Resin” (manufactured by Mitsubishi Chemical Corporation) and “Amberlite
Examples include "AD Resin" (manufactured by Rohm and Haas Co., Ltd.) and "Duolite S Resin" (manufactured by Diamond Shamrotsuta Co., Ltd.).

前記抽出液と合成吸着樹脂との接触は、バッチ法または
カラム法のいずれの方法を使用してもよい。バッチ法の
場合は、適当な容器に合成吸着樹脂を入れ、適宜撹拌す
る等、一般的な手法により行うことができる。カラム法
の場合は、通常行われる手法により達成でき、溶出速度
は、カラムの大きさ、使用する溶出溶媒等の種々の条件
を考1・放して適宜選択することができる。上記、バッ
チ法およびカラム法ともに物理吸着であるため、温度と
しては室温程度が望ましい。
The extract and the synthetic adsorption resin may be contacted by either a batch method or a column method. In the case of a batch method, the synthetic adsorption resin can be placed in a suitable container and stirred as appropriate, or by other common methods. In the case of a column method, this can be achieved by a commonly used method, and the elution rate can be appropriately selected by considering various conditions such as the size of the column and the elution solvent used. Since both the batch method and the column method described above involve physical adsorption, the temperature is preferably about room temperature.

次に、合成吸着樹脂に吸着したイソフラボン誘導体を有
機溶媒または有機溶媒と水との混合溶媒を用いて溶出さ
せる。この場合、バッチ法、カラム法のいずれを使用し
ても良く、溶出に用いる溶媒としては、有機溶媒または
有機溶媒と水との混合溶媒を用い得る。溶出溶媒の種類
、濃度、量はカラム法で行うかバッチ法で行うか、また
、用いる合成吸着樹脂の種類およびm等の種々の条件を
考慮して適宜選択する。
Next, the isoflavone derivative adsorbed on the synthetic adsorption resin is eluted using an organic solvent or a mixed solvent of an organic solvent and water. In this case, either a batch method or a column method may be used, and the solvent used for elution may be an organic solvent or a mixed solvent of an organic solvent and water. The type, concentration, and amount of the elution solvent are appropriately selected in consideration of various conditions such as whether the elution is performed by a column method or a batch method, and the type and m of the synthetic adsorption resin used.

有機溶媒の具体例としては、メタノール、エタノール、
イソプロパツール、アセトン等が挙げられるが、好まし
くはアルコール類またはアルコール類と水との混合溶媒
、さらに好ましくはメタノールまたはメタノールと水と
の混合溶媒が挙げられる。
Specific examples of organic solvents include methanol, ethanol,
Examples include isopropanol and acetone, preferably alcohols or a mixed solvent of alcohols and water, and more preferably methanol or a mixed solvent of methanol and water.

バッチ法により得られた溶出液、またはカラム法により
得られた溶出液に複数の成分が含まれている場合には、
通常用いられる分離精製の手法(例えば、向流分配、再
結晶、カラムクロマトグラフィー等)により、精製し、
単離することができる。
If the eluate obtained by the batch method or the eluate obtained by the column method contains multiple components,
Purified by commonly used separation and purification techniques (e.g. countercurrent distribution, recrystallization, column chromatography, etc.),
Can be isolated.

本発明のイソフラボン誘導体の製造方法で使用した合成
吸着樹脂は、適当な有機溶媒(例えば、アルコール系、
アセトン系有機溶媒等)または、アルカリ剤(例えば、
水酸化ナトリウム、水酸化カリウム等)により洗浄再生
することにより、繰り返し使用が可能であり、非常に経
済的である。
The synthetic adsorption resin used in the method for producing isoflavone derivatives of the present invention can be used in a suitable organic solvent (e.g., alcohol-based,
acetone-based organic solvents, etc.) or alkaline agents (e.g.
By washing and regenerating with sodium hydroxide, potassium hydroxide, etc., it can be used repeatedly and is very economical.

[実施例] 次に実施例を示して本発明を更に詳しく説明するが、本
発明はこれにより何ら制限されるものではない。
[Examples] Next, the present invention will be explained in more detail with reference to Examples, but the present invention is not limited thereto.

実施例1 細切した葛根2.2kgに水7又を加え、水の中で葛根
を粉砕して得た溶液をシ戸布でシ濾過し一晩放置した後
、その上清2QOJを5N水酸化ナトリウム溶液でpl
+6.0に調整した。次に、200Δのメタノールと2
00−の水で洗浄活性化させたスチレン−ジビニルベン
ゼン重合樹脂(三菱化成工業株式会社製、ダイヤイオン
HP−20)80dを充填した樹脂塔に、前記の溶液を
添加し、樹脂塔内をl O11jJ / minで通過
させ、次いで600−の水、次いで10%メタノール水
溶液を加えて洗浄を行った。洗浄後、樹脂塔にまず70
%メタノール水溶液200Δを溶出速度10mfJ/m
inで通過させ褐色のブエラリン、ダイズイン含有溶液
を、次にメタノール80゛−を通過させ褐色のダイゼイ
ン含有溶液を得た。
Example 1 Add 7 drops of water to 2.2 kg of finely chopped arrowroot, pulverize the arrowroot in water, filter the obtained solution with a cloth, leave it overnight, and then add 2QOJ of the supernatant to 5N water. pl with sodium oxide solution
Adjusted to +6.0. Next, 200Δ methanol and 2
The above solution was added to a resin tower filled with 80 d of styrene-divinylbenzene polymer resin (Diaion HP-20, manufactured by Mitsubishi Chemical Industries, Ltd.) which had been washed and activated with 00- water, and the inside of the resin tower was It was passed through at 11jJ/min, and then washed by adding 600-ml water and then 10% methanol aqueous solution. After washing, first add 70% to the resin tower.
% methanol aqueous solution 200Δ at elution rate 10 mfJ/m
A brown solution containing buerarin and daidzein was passed through the solution, and then 80° of methanol was passed through the solution to obtain a brown solution containing daidzein.

実施例2 上記実施例1で得られた葛根抽出液の上清500、−d
をガーゼでア過し、5N水酸化ナトリウム溶液でpH6
,0に調整した。次に、400mf!のメタノールと4
00−の水で活性化させたスチレンーンビニルベンゼン
重合樹脂(三菱化成工業株式会社製、ダイヤイオンHP
−20)200−を前記の溶液に添加し、時々撹拌しな
がら室温で4時間放置した。この混合液を柄出ロートで
I過して、その残渣をカラムに移し、400−の水を加
えて洗浄を行った後、カラムに70%メタノール水溶液
2又を溶出速度50111/minで通過させ褐色のプ
エラリン、ダイズイン含有溶液を得、次に、メタノール
245文を溶出速度50mfJ/minで通過させて褐
色のダイゼイン含有溶液を得た。
Example 2 Supernatant 500, -d of arrowroot extract obtained in Example 1 above
Passed through gauze and diluted with 5N sodium hydroxide solution to pH 6.
, adjusted to 0. Next, 400mf! of methanol and 4
Styrene-vinylbenzene polymer resin activated with 00-water (manufactured by Mitsubishi Chemical Corporation, Diaion HP)
-20) 200- was added to the above solution and left at room temperature for 4 hours with occasional stirring. This mixture was passed through a patterned funnel, the residue was transferred to a column, and washed by adding 400 ml of water. Two portions of a 70% aqueous methanol solution were passed through the column at an elution rate of 50111/min. A brown solution containing puerarin and daidzein was obtained, and then 245 methanol was passed through the solution at an elution rate of 50 mfJ/min to obtain a brown solution containing daidzein.

Claims (1)

【特許請求の範囲】[Claims] 葛根の抽出液をそのままもしくは溶媒を留去して合成吸
着樹脂に接触させて、イソフラボン誘導体を吸着せしめ
、次いで有機溶媒または有機溶媒と水との混合溶媒を用
いて該合成樹脂から溶出させてイソフラボン誘導体を得
ることを特徴とするイソフラボン誘導体の製造方法。
The extract of kudzu root is brought into contact with a synthetic adsorption resin, either as it is or after the solvent is distilled off, to adsorb isoflavone derivatives.Then, the isoflavone derivatives are eluted from the synthetic resin using an organic solvent or a mixed solvent of an organic solvent and water. A method for producing an isoflavone derivative, the method comprising obtaining a derivative.
JP26612485A 1985-11-28 1985-11-28 Production of isoflavone derivative Granted JPS62126185A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26612485A JPS62126185A (en) 1985-11-28 1985-11-28 Production of isoflavone derivative

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26612485A JPS62126185A (en) 1985-11-28 1985-11-28 Production of isoflavone derivative

Publications (2)

Publication Number Publication Date
JPS62126185A true JPS62126185A (en) 1987-06-08
JPH0421669B2 JPH0421669B2 (en) 1992-04-13

Family

ID=17426658

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26612485A Granted JPS62126185A (en) 1985-11-28 1985-11-28 Production of isoflavone derivative

Country Status (1)

Country Link
JP (1) JPS62126185A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5919921A (en) * 1996-06-11 1999-07-06 Protein Technologies International, Inc. Recovery of isoflavones from soy molasses
US6083553A (en) * 1998-06-05 2000-07-04 Protein Technologies International, Inc. Recovery of isoflavones from soy molasses
JP2002097149A (en) * 2000-09-20 2002-04-02 Noevir Co Ltd Skin care preparation
US6703051B1 (en) 1998-10-13 2004-03-09 Solae, Llc Process for separating and recovering protein and isoflavones from a plant material
CN1296049C (en) * 2004-02-25 2007-01-24 北京同仁堂科技发展股份有限公司制药厂 Sustained release preparation for treating cardiovascular diseases, adn preparation method, quality control method
CN103145858A (en) * 2013-03-19 2013-06-12 湖南省强生药业有限公司 Method for extracting flavone-rich pueraria starch from pueraria lobata
CN103554276A (en) * 2013-10-15 2014-02-05 温天文 Technological process for extracting starch, cellulose and general flavone in root of kudzu vine by use of organic membrane

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5133167A (en) * 1974-06-05 1976-03-22 Sarubadooru Montagyuto Gy Hose
JPS59187746A (en) * 1983-04-11 1984-10-24 Hayashibara Biochem Lab Inc Beverage and its preparation

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5133167A (en) * 1974-06-05 1976-03-22 Sarubadooru Montagyuto Gy Hose
JPS59187746A (en) * 1983-04-11 1984-10-24 Hayashibara Biochem Lab Inc Beverage and its preparation

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6706292B2 (en) 1996-06-11 2004-03-16 Solae, Llc Recovery of isoflavones from soy molasses
US6323018B1 (en) 1996-06-11 2001-11-27 Protein Technologies Int'l Lnc. Recovery of isoflavones from soy molasses
US5919921A (en) * 1996-06-11 1999-07-06 Protein Technologies International, Inc. Recovery of isoflavones from soy molasses
US6495141B2 (en) 1996-06-11 2002-12-17 Protein Technologies International, Inc. Recovery of isoflavones from soy molasses
US6664382B2 (en) 1996-06-11 2003-12-16 Solae, Llc Recovery of isoflavones from soy molasses
US6680381B1 (en) 1996-06-11 2004-01-20 Solae, Llc Recovery of isoflavones from soy molasses
US6083553A (en) * 1998-06-05 2000-07-04 Protein Technologies International, Inc. Recovery of isoflavones from soy molasses
US6703051B1 (en) 1998-10-13 2004-03-09 Solae, Llc Process for separating and recovering protein and isoflavones from a plant material
JP2002097149A (en) * 2000-09-20 2002-04-02 Noevir Co Ltd Skin care preparation
CN1296049C (en) * 2004-02-25 2007-01-24 北京同仁堂科技发展股份有限公司制药厂 Sustained release preparation for treating cardiovascular diseases, adn preparation method, quality control method
CN103145858A (en) * 2013-03-19 2013-06-12 湖南省强生药业有限公司 Method for extracting flavone-rich pueraria starch from pueraria lobata
CN103145858B (en) * 2013-03-19 2015-07-01 湖南省强生药业有限公司 Method for extracting flavone-rich pueraria starch from pueraria lobata
CN103554276A (en) * 2013-10-15 2014-02-05 温天文 Technological process for extracting starch, cellulose and general flavone in root of kudzu vine by use of organic membrane

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