JPH0714927B2 - Method for producing isoflavone compound - Google Patents
Method for producing isoflavone compoundInfo
- Publication number
- JPH0714927B2 JPH0714927B2 JP8318588A JP8318588A JPH0714927B2 JP H0714927 B2 JPH0714927 B2 JP H0714927B2 JP 8318588 A JP8318588 A JP 8318588A JP 8318588 A JP8318588 A JP 8318588A JP H0714927 B2 JPH0714927 B2 JP H0714927B2
- Authority
- JP
- Japan
- Prior art keywords
- soybean
- isoflavone
- isoflavone compound
- aglycone
- 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.)
- Expired - Lifetime
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- Saccharide Compounds (AREA)
- Pyrane Compounds (AREA)
Description
【発明の詳細な説明】 <産業上の利用分野> 本発明は大豆からイソフラボン化合物、特にそのアグリ
コン類を多量に含むイソフラボン化合物の製造法に関す
るものである。TECHNICAL FIELD The present invention relates to a process for producing an isoflavone compound from soybean, particularly an isoflavone compound containing a large amount of aglycones thereof.
<従来の技術及び問題点> 大豆にはダイジン、グリシチン、ゲニスチン、ダイゼイ
ン、ゲニステイン等のイソフラボン化合物が含まれてお
り、その生理活性作用はエストロゲン作用は、抗酸化、
抗溶血作用、抗菌作用、抗脂血、抗コレステロール作用
が知られており、また最近ではガン細胞の分化誘導作
用、ガン遺伝子阻害作用等、制ガン効果も確認され、そ
の有用性が注目されている。<Conventional Technology and Problems> Soybean contains isoflavone compounds such as daidzin, glycitin, genistin, daidzein, and genistein. Its physiological activity is estrogen, antioxidant,
Anti-hemolytic action, anti-bacterial action, anti-lipidemia, anti-cholesterol action are known, and recently, anti-cancer effects such as cancer cell differentiation inducing action and oncogene inhibitory action have been confirmed, and their usefulness has been noted. There is.
これらイソフラボン化合物のうち制ガン作用等の医薬的
な効果は配糖体ではなく、ダイゼイン、ゲニステイン等
のアグリコンが主となっている。Among these isoflavone compounds, aglycones such as daidzein and genistein are mainly used for the medicinal effects such as carcinostatic action, not glycosides.
大豆の抽出液からイソフラボン化合物を得る方法とし
て、例えば特開昭62−126186号公報が挙げられている
が、大豆中では95%以上が配糖体として存在している
為、この方法によって得られるイソフラボン化合物は配
糖体が主体となり、アグリコンは極めて少量しか得るこ
とができない。As a method for obtaining an isoflavone compound from an extract of soybean, for example, JP-A-62-126186 is mentioned. However, since 95% or more of soybean exists as a glycoside, it can be obtained by this method. The isoflavone compound is mainly composed of glycosides, and it is possible to obtain an extremely small amount of aglycone.
<問題点を解決するための手段> 本発明者等はイソフラボン化合物のうちでも有用性が極
めて高いアグリコンを安価かつ大量に得る方法について
検討したところ、大豆のイソフラボンは大豆中のβ−グ
ルコシダーゼの作用により容易に糖結合を切断した、そ
のアグリコンへ変換すること、その変換は50℃、pH6.3
で最大となるという知見を得た。<Means for Solving Problems> The inventors of the present invention investigated a method for inexpensively obtaining a large amount of highly useful aglycone among isoflavone compounds. As a result, soy isoflavone is an action of β-glucosidase in soybean. The sugar bond was easily cleaved to convert it to its aglycone. The conversion was 50 ℃, pH6.3.
We obtained the knowledge that
本発明はこの様な知見に基づき成されたものであって、
大豆抽出液あるいは大豆磨砕物からイソフラボン化合物
を製造するに際し、大豆中のβ−グルコシダーゼ活性が
最大となるように、浸漬工程、磨砕工程あるいは磨砕後
の酵素反応工程のいずれか、あるいは2以上の工程にお
いて、大豆あるいは大豆磨砕物を45〜55℃に加熱するこ
とを特徴とするイソフラボン化合物の製造法である。The present invention was made based on such findings,
At the time of producing an isoflavone compound from a soybean extract or a soybean ground product, any one of dipping step, grinding step or enzymatic reaction step after grinding, or two or more so that β-glucosidase activity in soybean is maximized In the step of 1, the soybean or ground soybean product is heated to 45 to 55 ° C, which is a method for producing an isoflavone compound.
以下、本発明を具体的に説明する。Hereinafter, the present invention will be specifically described.
原料となる大豆は酵素の失活していないものならば、ど
の様なものでもよく、例えば低変性脱脂大豆粉、ひき割
り大豆、脱皮大豆、丸大豆等を用いることができる。Any soybean may be used as a raw material as long as the enzyme is not deactivated, and for example, low-denaturation defatted soybean powder, crushed soybean, dehulled soybean, whole soybean, and the like can be used.
これらの大豆の抽出液からイソフラボン化合物を製造す
るには、大豆を5〜10倍の45〜55℃の温水に浸漬し、そ
の浸漬水を抽出液として精製原料とするが、浸漬水はダ
イゼインの比率が大豆中よりも10%程度多くなるので、
好適な精製原料と成り得る。In order to produce an isoflavone compound from these soybean extracts, soybeans are soaked in 5 to 10 times warm water at 45 to 55 ° C., and the soaked water is used as a refined raw material for soaking. Since the ratio is about 10% higher than in soybeans,
It can be a suitable refined raw material.
また大豆の磨砕物からイソフラボン化合物を製造する場
合には、上記の様に浸漬した大豆を浸漬水と共に磨砕す
るか、あるいは常温水で浸漬して、その浸漬大豆を45〜
55℃で磨砕するか、あるいは磨砕後45〜55℃に加熱して
酵素反応させればよいが、好適には浸漬を45〜55℃で行
ない、これを浸漬水と共に45〜55℃で磨砕し、得られた
磨砕物45〜55℃で数時間保持する。こうすることにより
大豆中のアグリコンの比率が大きく上昇する。When producing an isoflavone compound from a ground soybean product, the soybean soaked as described above is ground with soaking water, or soaked in room temperature water, and the soybean soup is 45-
It may be ground at 55 ° C, or after grinding, it may be heated to 45 to 55 ° C to cause an enzymatic reaction, but preferably the immersion is carried out at 45 to 55 ° C and this is carried out at 45 to 55 ° C together with immersion water. Grind and hold the resulting grind at 45-55 ° C for several hours. This greatly increases the percentage of aglycone in soybeans.
こうして得られた大豆抽出液あるいは大豆磨砕物を精製
原料として用いるが、イソフラボン化合物の精製は2通
りの方法がある。The soybean extract or soybean ground product thus obtained is used as a purification raw material, and there are two methods for purification of the isoflavone compound.
1つは溶媒による精製で精製用原料、即ち大豆浸漬水あ
るいは大豆磨砕物を熱風乾燥、凍結乾燥等により粉末化
し、これのn−ヘキサンあるいは石油エーテルで脱脂
し、その残渣を乾燥後エチルエーテルで抽出してイソフ
ラボンアグリコンのみを得る方法である。One is purification with a solvent, which is a raw material for refining, that is, soybean soaked water or ground soybeans, is pulverized by hot air drying, freeze drying, etc., degreased with n-hexane or petroleum ether, and the residue is dried with ethyl ether. It is a method of extracting only isoflavone aglycone.
もう一方は精製用原料の粉末化物を含水アルコールでイ
ソフラボン化合物を還流抽出し、その抽出液を常法によ
り濃縮、乾固させ、それを少量の含水アルコールに溶解
し、これを逆相系の樹脂、例えばYMC−GEL ODS−Aタ
イプ60−01((株)山村化学研究所製)やダイヤイオン
HP−20(三菱化成工業(株)製)などに吸着させた後、
十分水洗し、20%程度の含水アルコールでフェノール酸
を溶出させ、次いで80%含水アルコールでアグリコンを
豊富に含むイソフラボン化合物区分を得る方法である。
又、水洗の後、40%程度の含水アルコールで配糖体画分
を流出させれば、80%含水アルコールの溶出により、ア
グリコン区分のみを得ることもできる。On the other hand, the isoflavone compound is reflux-extracted with a hydrous alcohol from the powdered raw material for purification, and the extract is concentrated and dried to dryness by a conventional method, and then dissolved in a small amount of hydrous alcohol. , YMC-GEL ODS-A type 60-01 (manufactured by Yamamura Chemical Laboratory Co., Ltd.) and Diaion
After adsorbing on HP-20 (manufactured by Mitsubishi Kasei Co., Ltd.) etc.,
It is a method of thoroughly washing with water, eluting phenolic acid with about 20% hydrous alcohol, and then obtaining an isoflavone compound category rich in aglycone with 80% hydrous alcohol.
Also, after washing with water, if the glycoside fraction is flown out with about 40% hydrous alcohol, it is possible to obtain only the aglycone category by elution of 80% hydrous alcohol.
尚、ここで用いられる逆相系の樹脂は有機溶媒、例えば
アルコール系、アセトン系等で洗浄再生が容易であり、
繰り返し利用できる。Incidentally, the reverse phase resin used here is easy to wash and regenerate with an organic solvent such as alcohol or acetone.
Can be used repeatedly.
又、精製用原料を粉末化しないで直接樹脂に吸着させて
精製することも可能であり、浸漬水の場合には、そのま
ま、又磨砕物の場合には常法により濾過した濾液あるい
は遠心分離した上澄液を逆相系に樹脂に接触させ、以下
上記と同様に精製する。It is also possible to directly adsorb the purification raw material onto the resin without pulverizing it for purification, and in the case of immersion water, as it is, or in the case of ground material, filtrate filtered by a conventional method or centrifuged. The supernatant is brought into contact with the resin in a reverse phase system and then purified in the same manner as above.
以下、実験例を示し本発明の効果を説明する。The effects of the present invention will be described below with reference to experimental examples.
実験例1 脱皮大豆を5倍量の20〜80℃の水に6時間浸漬し、その
浸漬水と浸漬大豆を直ちに冷却、凍結させる。それを凍
結乾燥機にて乾燥、粉末化し、その一定量を80%メタノ
ールで還流抽出し、定容したものの一定量を高速液体ク
ロマトグラフィー(Waters社209D型)にて分析した。Experimental Example 1 Hulled soybeans are immersed in 5 times the amount of water at 20 to 80 ° C. for 6 hours, and the soaked water and the soybeans are immediately cooled and frozen. It was dried with a freeze drier, pulverized, a certain amount of the mixture was refluxed and extracted with 80% methanol, and a fixed amount was analyzed by high performance liquid chromatography (Model 209D manufactured by Waters).
結果を第1表に示す。The results are shown in Table 1.
実験例2 脱皮大豆をpH5.5〜11に調整した5倍量の50℃の温水に
2時間浸漬し、その浸漬水をpHを酸性にして後、直ちに
0.45μmのフィルターにて濾過後、実験例1と同様に高
速液体クロマトグラフィーにて分析した。 Experimental Example 2 Dehulled soybeans were immersed in 5 times the amount of warm water at 50 ° C. adjusted to pH 5.5 to 11 for 2 hours, and the immersion water was acidified immediately and immediately thereafter.
After filtration with a 0.45 μm filter, analysis was performed by high performance liquid chromatography in the same manner as in Experimental Example 1.
結果を第2表に示す。The results are shown in Table 2.
実験例1、2の結果から明らかな様に浸漬温度45〜55℃
で、又浸漬水のpH6.3でイソフラボンアグリコンへの交
換が最大となる。 As is clear from the results of Experimental Examples 1 and 2, the immersion temperature is 45 to 55 ° C.
At pH 6.3, the exchange of isoflavone aglycone is maximized.
<実施例> 以下に実施例を示す。<Examples> Examples are shown below.
実施例1 脱皮大豆を5kgを50℃の温水25中に浸漬し、50℃で保
温しながら2時間浸漬した。Example 1 5 kg of dehulled soybeans were dipped in warm water 25 at 50 ° C. and soaked for 2 hours while keeping the temperature at 50 ° C.
次いで、その浸漬水をエボパレーターにて濃縮、乾固
し、精製原料450gを得た。これをソックスレー抽出器を
使い、n−ヘキサンにて脱脂した。次いで、その残渣を
十分乾燥した後、エチルエーテルにて抽出し、イソフラ
ボンのアグリコン0.5gを得た。Then, the immersion water was concentrated with an evaporator and dried to obtain 450 g of a purified raw material. This was degreased with n-hexane using a Soxhlet extractor. Then, the residue was sufficiently dried and then extracted with ethyl ether to obtain 0.5 g of isoflavone aglycone.
実施例2 実施例1と同様に浸漬した脱皮大豆を浸漬水と共に50℃
にて磨砕し、その磨砕物を50℃、1時間保持したものを
凍結乾燥機にて乾燥、粉末化し、精製原料4.1kgを得
た。これを実施例1と同様に、n−ヘキサンによる脱
脂、エチルエーテルによるアグリコンの抽出を行ない、
イソフラボンアグリコン7.2gを得た。50℃の磨砕及びそ
の温度での1時間保持によりアグリコン率は60%以上に
なった。Example 2 Dehulled soybeans dipped in the same manner as in Example 1 together with immersion water at 50 ° C.
Was ground for 1 hour, dried at a freeze dryer and powdered to obtain 4.1 kg of purified raw material. In the same manner as in Example 1, degreasing with n-hexane and extraction of aglycone with ethyl ether were carried out.
7.2 g of isoflavone aglycone was obtained. The aglycone ratio was 60% or more after milling at 50 ° C and holding at that temperature for 1 hour.
実施例3 低変性脱脂大豆(日清ソーヤフラワー)10kgに50℃の
水、50を加え、1時間撹拌した。これをスプレードラ
イにて熱風乾燥し、精製原料を得た。精製原料に対し5
倍量の80%熱メタノールによりイソフラボン類を抽出
し、減圧乾固して粗イソフラボン画分103gを得た。これ
を少量のメタノールに再溶解し、充填剤としてODS−A
タイプ60−01((株)山村化学研究所製)をつめたφ70
mm×100cmのカラムに通して吸着させた。Example 3 50 kg of water at 50 ° C. was added to 10 kg of low-denaturation defatted soybean (Nisshin Soya Flower) and stirred for 1 hour. This was dried with hot air by spray drying to obtain a purified raw material. 5 for refined raw materials
Isoflavones were extracted with a double amount of 80% hot methanol and dried under reduced pressure to obtain 103 g of a crude isoflavone fraction. This was redissolved in a small amount of methanol and used as a packing material for ODS-A.
Φ70 packed with Type 60-01 (made by Yamamura Chemical Laboratory Co., Ltd.)
It was adsorbed by passing through a column of mm × 100 cm.
次いで、40%のメタノールでフェノール酸やイソフラボ
ン配糖体画分を流出させ、除去し、次いで80%メタノー
ルで溶出し、これを減圧乾固したところ、アグリコン9.
5gを得た。Next, the phenolic acid and isoflavone glycoside fractions were flown out with 40% methanol, removed, and then eluted with 80% methanol, which was evaporated to dryness under reduced pressure, and aglycone 9.
Got 5g.
実施例4 脱皮大豆を実施例1と同様の方法で浸漬処理して得た浸
漬水25に、合成吸着剤ダイヤイオンHP−20(三菱化成
工業(株)製)1kgを加え、1時間攪拌しながら、イソ
フラボン化合物を吸着させた。次いで、その樹脂を濾別
して、20%のエタノールで洗浄してフェノール酸を除去
し、次いで80%エタノールで溶出させイソフラボン化合
物を得た。これの減圧乾燥後の重量は1.1gであった。こ
のイソフラボン化合物中には約40%のアグリコンが含有
していた。Example 4 1 kg of the synthetic adsorbent Diaion HP-20 (manufactured by Mitsubishi Kasei Co., Ltd.) was added to immersion water 25 obtained by dipping dehulled soybeans in the same manner as in Example 1 and stirred for 1 hour. While adsorbing the isoflavone compound. Then, the resin was filtered off, washed with 20% ethanol to remove phenolic acid, and then eluted with 80% ethanol to obtain an isoflavone compound. The weight of this after drying under reduced pressure was 1.1 g. The isoflavone compound contained about 40% aglycone.
Claims (1)
ラボン化合物を製造するに際し、大豆中のβ−グルコシ
ダーゼ活性が最大となるように、浸漬工程、磨砕工程あ
るいは磨砕後の酵素反応工程のいずれか、あるいは2以
上の工程において、大豆あるいは大豆磨砕物を45〜55℃
に加熱することを特徴とするイソフラボン化合物の製造
法。1. When producing an isoflavone compound from a soybean extract or a soybean ground product, any one of a dipping step, a grinding step and an enzyme reaction step after grinding so that the β-glucosidase activity in soybean is maximized. Or, in two or more steps, soybeans or ground soybeans at 45 to 55 ° C
A method for producing an isoflavone compound, which comprises heating to
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8318588A JPH0714927B2 (en) | 1988-04-06 | 1988-04-06 | Method for producing isoflavone compound |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8318588A JPH0714927B2 (en) | 1988-04-06 | 1988-04-06 | Method for producing isoflavone compound |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01258669A JPH01258669A (en) | 1989-10-16 |
JPH0714927B2 true JPH0714927B2 (en) | 1995-02-22 |
Family
ID=13795260
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8318588A Expired - Lifetime JPH0714927B2 (en) | 1988-04-06 | 1988-04-06 | Method for producing isoflavone compound |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0714927B2 (en) |
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KR100729172B1 (en) * | 1999-12-15 | 2007-06-19 | 가부시키가이샤 아미노 압 가가쿠 | Novel substance originating in basidiomycete culture, process for producing the same and use thereof |
ES2251458T3 (en) * | 2000-01-11 | 2006-05-01 | Maabarot Projects Launching And Management Ltd. | FLAVONOID EXTRACTION. |
AUPQ504300A0 (en) | 2000-01-11 | 2000-02-03 | Biorex Health Limited | Extraction of flavonoids |
KR20020007553A (en) * | 2000-07-18 | 2002-01-29 | 조대연 | Process for producing aglycone isoflavones using microorganism |
US6326366B1 (en) | 2000-08-22 | 2001-12-04 | Protein Technologies International | Hormone replacement therapy |
AUPR363301A0 (en) | 2001-03-08 | 2001-04-05 | Novogen Research Pty Ltd | Dimeric isoflavones |
WO2003000674A1 (en) * | 2001-06-21 | 2003-01-03 | Fuji Oil Company,Limited | Process for producing soluble isoflavone-containing composition |
CN111560406B (en) * | 2020-04-27 | 2023-05-16 | 黑龙江大学 | Method for producing flavonoid substances from external products such as soybean for vegetable by fermenting bacillus natto |
-
1988
- 1988-04-06 JP JP8318588A patent/JPH0714927B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH01258669A (en) | 1989-10-16 |
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