JPH0352447B2 - - Google Patents
Info
- Publication number
- JPH0352447B2 JPH0352447B2 JP57117854A JP11785482A JPH0352447B2 JP H0352447 B2 JPH0352447 B2 JP H0352447B2 JP 57117854 A JP57117854 A JP 57117854A JP 11785482 A JP11785482 A JP 11785482A JP H0352447 B2 JPH0352447 B2 JP H0352447B2
- Authority
- JP
- Japan
- Prior art keywords
- soybean saponin
- methanol
- soy sauce
- extract
- 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
- 229930182490 saponin Natural products 0.000 claims description 51
- 150000007949 saponins Chemical class 0.000 claims description 51
- 235000010469 Glycine max Nutrition 0.000 claims description 48
- 244000068988 Glycine max Species 0.000 claims description 47
- 239000001397 quillaja saponaria molina bark Substances 0.000 claims description 47
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 32
- 235000013555 soy sauce Nutrition 0.000 claims description 26
- 238000000605 extraction Methods 0.000 claims description 14
- 238000001179 sorption measurement Methods 0.000 claims description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- 239000003960 organic solvent Substances 0.000 claims description 13
- 229920005989 resin Polymers 0.000 claims description 11
- 239000011347 resin Substances 0.000 claims description 11
- 238000000926 separation method Methods 0.000 claims description 10
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 238000005192 partition Methods 0.000 claims description 6
- 238000004587 chromatography analysis Methods 0.000 claims description 3
- 238000005238 degreasing Methods 0.000 claims description 3
- 238000001556 precipitation Methods 0.000 claims description 3
- 238000002336 sorption--desorption measurement Methods 0.000 claims description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 66
- 235000017709 saponins Nutrition 0.000 description 49
- 239000002904 solvent Substances 0.000 description 24
- 239000000284 extract Substances 0.000 description 19
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 15
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 12
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 12
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 10
- 238000001914 filtration Methods 0.000 description 9
- 239000007788 liquid Substances 0.000 description 9
- 238000000034 method Methods 0.000 description 9
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 8
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 8
- 239000000126 substance Substances 0.000 description 8
- 239000002244 precipitate Substances 0.000 description 7
- 239000000203 mixture Substances 0.000 description 5
- 239000000741 silica gel Substances 0.000 description 5
- 229910002027 silica gel Inorganic materials 0.000 description 5
- -1 soy sauce oil Chemical class 0.000 description 5
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 4
- 239000006227 byproduct Substances 0.000 description 4
- 238000005119 centrifugation Methods 0.000 description 4
- 239000007858 starting material Substances 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 239000005909 Kieselgur Substances 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- 150000002632 lipids Chemical class 0.000 description 3
- 239000000401 methanolic extract Substances 0.000 description 3
- 238000010992 reflux Methods 0.000 description 3
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 150000001298 alcohols Chemical class 0.000 description 2
- 229920001429 chelating resin Polymers 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 238000003795 desorption Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 229940079593 drug Drugs 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- 239000000469 ethanolic extract Substances 0.000 description 2
- 150000002170 ethers Chemical class 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 150000008282 halocarbons Chemical class 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 150000002576 ketones Chemical class 0.000 description 2
- 239000012046 mixed solvent Substances 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000004809 thin layer chromatography Methods 0.000 description 2
- 239000003643 water by type 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
- ZAFNJMIOTHYJRJ-UHFFFAOYSA-N Diisopropyl ether Chemical compound CC(C)OC(C)C ZAFNJMIOTHYJRJ-UHFFFAOYSA-N 0.000 description 1
- 239000004278 EU approved seasoning Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 230000003266 anti-allergic effect Effects 0.000 description 1
- 230000003110 anti-inflammatory effect Effects 0.000 description 1
- 230000000767 anti-ulcer Effects 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 230000004071 biological effect Effects 0.000 description 1
- KTUQUZJOVNIKNZ-UHFFFAOYSA-N butan-1-ol;hydrate Chemical compound O.CCCCO KTUQUZJOVNIKNZ-UHFFFAOYSA-N 0.000 description 1
- SIHHLZPXQLFPMC-UHFFFAOYSA-N chloroform;methanol;hydrate Chemical compound O.OC.ClC(Cl)Cl SIHHLZPXQLFPMC-UHFFFAOYSA-N 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 210000003298 dental enamel Anatomy 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 238000002481 ethanol extraction Methods 0.000 description 1
- 239000002024 ethyl acetate extract Substances 0.000 description 1
- 238000003810 ethyl acetate extraction Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 235000011194 food seasoning agent Nutrition 0.000 description 1
- 230000002949 hemolytic effect Effects 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 238000004811 liquid chromatography Methods 0.000 description 1
- 238000003808 methanol extraction Methods 0.000 description 1
- GBMDVOWEEQVZKZ-UHFFFAOYSA-N methanol;hydrate Chemical compound O.OC GBMDVOWEEQVZKZ-UHFFFAOYSA-N 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 235000011118 potassium hydroxide Nutrition 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000010898 silica gel chromatography Methods 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Saccharide Compounds (AREA)
- Medicines Containing Plant Substances (AREA)
Description
【発明の詳細な説明】
本発明は、醤油製造過程で副産物として得られ
る醤油粕を出発原料として、大豆サポニンを製造
する方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing soybean saponin using as a starting material soy sauce lees obtained as a by-product in the soy sauce production process.
一般にサポニンは乳化剤や分散剤として化粧品
や保健薬に、また食品工業においても利用されて
いる。最近、医薬学領域においてサポニン生薬が
見直されるようになり、その抗炎症効果、抗潰瘍
効果、抗アレルギー効果なども利用されるに到つ
ている。 Generally, saponins are used as emulsifiers and dispersants in cosmetics and health drugs, and also in the food industry. Recently, saponin crude drugs have been reconsidered in the pharmaceutical field, and their anti-inflammatory, anti-ulcer, and anti-allergic effects have also come to be utilized.
大豆サポニンはサポニンの生物学的特性である
溶血作用が最も弱い、いわゆる毒性の低いサポニ
ンとして古くから知られているが、大豆からの分
離工程が複雑で経済的に不利であることが、実用
上の欠点とされている。 Soybean saponin has long been known as a low-toxic saponin with the weakest hemolytic effect, which is a biological property of saponins, but the separation process from soybeans is complicated and economically disadvantageous, making it difficult to use in practical applications. It is considered a drawback.
本発明者らは、この大豆サポニンを醤油製造工
程で副生する醤油粕を出発原料として工業的に有
利に製造しうることを見出した。 The present inventors have discovered that this soybean saponin can be industrially advantageously produced using soy sauce lees, which is a by-product in the soy sauce manufacturing process, as a starting material.
本発明は、醤油粕又はこれを有機溶剤で脱脂処
理して得られる脱脂醤油粕に、水及び/又は低級
アルコールを加えて抽出し、得られた抽出部に、
有機溶剤による分配抽出、非イオン性吸着樹脂に
よる吸着脱離、分別沈殿及びクロマトグラフイよ
り選ばれた少なくとも1種の分離手段を施して大
豆サポニンを分離することを特徴とする、大豆サ
ポニンの製造法である。 The present invention involves adding water and/or lower alcohol to soy sauce lees or defatted soy sauce lees obtained by degreasing this with an organic solvent, and extracting the resulting extracted portion.
Production of soybean saponin, characterized in that soybean saponin is separated by applying at least one separation method selected from partition extraction with an organic solvent, adsorption/desorption with a nonionic adsorption resin, fractional precipitation, and chromatography. It is the law.
本発明の出発原料として用いられる醤油粕は、
醤油製造工程において副生するものであつて、各
種の醤油ならびに醤油類似調味料の製造時に副生
する醤油粕を利用することができる。醤油粕は多
量の塩分を含むため、その利用も廃棄も困難とさ
れていたものであるが、本発明によればこれを利
用価値の高い工業製品に変えることができる。 The soy sauce lees used as the starting material of the present invention is
Soy sauce lees, which is a by-product in the soy sauce production process and is a by-product in the production of various soy sauces and soy sauce-like seasonings, can be used. Since soy sauce lees contains a large amount of salt, it has been difficult to use or dispose of it, but according to the present invention, it can be turned into an industrial product with high utility value.
醤油粕は通常は醤油油等の脂質を含んでいるの
で、予め有機溶剤を用いて常法により脱脂するこ
とにより得られる脱脂醤油粕として、使用するこ
とが好ましい。脱脂のための溶剤としては、例え
ばクロロホルムその他のハロゲン化炭化水素、エ
チルエーテル、イソプロピルエーテル等のエーテ
ル類、メタノール、エタノール等のアルコール
類、石油エーテル、ベンゼン等の炭化水素、アセ
トンその他のケトン類、酢酸エチルその他のエス
テル類又はこれらの溶剤の混合物を用いることが
できる。 Since soy sauce lees usually contains lipids such as soy sauce oil, it is preferably used as defatted soy sauce lees obtained by previously defatting the soy sauce lees in a conventional manner using an organic solvent. Examples of solvents for degreasing include chloroform and other halogenated hydrocarbons, ethers such as ethyl ether and isopropyl ether, alcohols such as methanol and ethanol, petroleum ether, hydrocarbons such as benzene, acetone and other ketones, Ethyl acetate and other esters or mixtures of these solvents can be used.
本発明によれば、醤油粕又は脱脂醤油粕を水及
び/又は低級アルコールで抽出する。この場合水
単独で抽出してもよいが、水性低級アルコール又
は低級アルコールを用いて抽出することが、抽出
効率の点でより好ましい。低級アルコールとして
は、例えばメタノール、エタノール、n−及びイ
ソプロパノール、n−ブタノール等が用いられる
が、大豆サポニンの収率の点からメタノール又は
水性エタノールが特に好ましい。抽出は常法によ
り、醤油粕又は脱脂醤油粕の重量当り5〜20倍量
の前記溶剤を使用し、常温又は加熱下でバツチ式
あるいは連続式の抽出装置を用いて行われる。 According to the present invention, soy sauce lees or defatted soy sauce lees is extracted with water and/or lower alcohol. In this case, extraction may be performed using water alone, but extraction using an aqueous lower alcohol or lower alcohol is more preferable in terms of extraction efficiency. As the lower alcohol, for example, methanol, ethanol, n- and isopropanol, n-butanol, etc. are used, but methanol or aqueous ethanol is particularly preferred from the viewpoint of the yield of soybean saponin. Extraction is carried out in a conventional manner using a batch-type or continuous-type extraction device at room temperature or under heating using the above-mentioned solvent in an amount of 5 to 20 times the weight of the soy sauce lees or defatted soy sauce lees.
次いでこうして得られた抽出液に、大豆サポニ
ンを分離するための前記の分離手段の1種又は2
種以上を組み合わせて適用する。この分離処理の
前に抽出液を例えば過、遠心分離その他の手段
で清澄化し、これに直接に非イオン性吸着樹脂に
よる吸着脱離を施す場合を除いて、通常は減圧下
に濃縮して溶剤を回収する。 Next, one or two of the above-mentioned separation means for separating soybean saponin are added to the extract thus obtained.
Apply in combination of more than one species. Prior to this separation process, the extract is clarified, for example, by filtration, centrifugation, or other means, and unless it is directly subjected to adsorption and desorption using a nonionic adsorption resin, it is usually concentrated under reduced pressure to remove the solvent. Collect.
前記の溶剤回収ののちに残部として得られる抽
出物から大豆サポニンを分離するには、まず有機
溶剤を用いる分配抽出法を適用できる。この方法
は大豆サポニンとその他の物質の有機溶剤に対す
る溶解度の差を利用するもので、例えば振盪抽出
法、これを連続的に行うパーホレーシヨン等の一
段分配法、ならびにこれらを組み合わせた多段分
配法等があげられる。 In order to separate soybean saponin from the extract obtained as a remainder after the above-mentioned solvent recovery, a partition extraction method using an organic solvent can be first applied. This method utilizes the difference in solubility of soybean saponin and other substances in organic solvents, and includes shaking extraction, one-stage distribution methods such as continuous perforation, and multi-stage distribution methods that combine these methods. can give.
この分配抽出法に用いられる有機溶剤は、例え
ばメタノール、エタノール等のアルコール類、ア
セトンその他のケトン類、エチルエーテル等のエ
ーテル類、酢酸エチルその他のエステル類、クロ
ロホルムその他のハロゲン化炭化水素類、石油エ
ーテル等の炭化水素類等から選ばれる2種以上の
相互に混和しない溶剤系であつて、水も用いられ
る。好ましい溶剤系の例は水とn−ブタノール、
2相に分離する各種割合のクロロホルム、メタノ
ール及び水の混合系の上相と下相等である。 Organic solvents used in this partition extraction method include alcohols such as methanol and ethanol, acetone and other ketones, ethers such as ethyl ether, ethyl acetate and other esters, chloroform and other halogenated hydrocarbons, petroleum It is a mutually immiscible solvent system of two or more selected from hydrocarbons such as ether, and water is also used. Examples of preferred solvent systems are water and n-butanol;
These are the upper and lower phases of a mixed system of chloroform, methanol, and water in various proportions that separate into two phases.
大豆サポニンを分離する他の方法としては、非
イオン性吸着樹脂による吸着脱離も利用できる。
非イオン性吸着樹脂としては、例えばスチレン系
吸着樹脂例えばサーバクロムXAD−2(サーバ社
製)、アンバーライトXAD−2(ロームアンドハ
ース社製)等が用いられる。水又は一般に30%
V/V未満の水性低級アルコールによる抽出液の
場合には、そのままで吸着樹脂に大豆サポニンを
選択的に吸着させることができる。より高濃度の
水性低級アルコール又は純粋な低級アルコールで
抽出した場合には、減圧濃縮して低級アルコール
を回収し又は加水することなどにより、抽出液中
の低級アルコールの濃度を一般に30%V/V未満
にしたのちに吸着を行う。次いで吸着樹脂に吸着
された大豆サポニンを低級アルコール又は高濃度
の水性低級アルコールを用いて脱離させることが
できる。 As another method for separating soybean saponin, adsorption/desorption using a nonionic adsorption resin can also be used.
As the nonionic adsorption resin, for example, styrene-based adsorption resins such as Serverchrome XAD-2 (manufactured by Server Co., Ltd.), Amberlite XAD-2 (manufactured by Rohm and Haas Co., Ltd.), etc. are used. water or generally 30%
In the case of an aqueous lower alcohol extract of less than V/V, soybean saponin can be selectively adsorbed to the adsorption resin as it is. When extracting with a higher concentration of aqueous lower alcohol or pure lower alcohol, the concentration of lower alcohol in the extract is generally reduced to 30% V/V by concentrating under reduced pressure to recover the lower alcohol or adding water. Adsorption is performed after reducing the amount to less than Then, the soybean saponin adsorbed on the adsorption resin can be desorbed using a lower alcohol or a highly concentrated aqueous lower alcohol.
なお抽出液又はその濃縮液中に大豆サポニン以
外の脂質が懸濁状態で比較的多量に共存する場合
には、大豆サポニンの吸着樹脂による選択的吸着
脱離が妨害されるので、予め静置分離あるいは珪
藻土等の過助剤を用いる過等により、これを
除去しておくと良好な結果が得られる。 Note that if a relatively large amount of lipids other than soybean saponin coexists in the extract or its concentrate in a suspended state, the selective adsorption and desorption of soybean saponin by the adsorption resin will be hindered, so static separation must be performed in advance. Alternatively, good results can be obtained by removing this by filtration using a supernatant such as diatomaceous earth.
分別沈殿法も前記の分配抽出法と同様に大豆サ
ポニンと他の物質の有機溶剤に対する溶解度の差
を利用するものとして、大豆サポニンの分離に有
利に適用することができる。すなわち大豆サポニ
ン及び他の物質を含む原料を、これらが溶解しう
る溶剤に溶解しておき、この溶液をどちらか一方
がより難溶な溶剤中に徐々に添加する。最終的に
沈殿した大豆サポニンを含む区分を採取し、その
他の物質の区分を除去する。この操作は同一の溶
剤系で繰り返してもよいが、別の溶剤系を選択
し、それらを組み合わせることによつて大豆サポ
ニンの分離をより効果的にすることもできる。 Similar to the partition extraction method described above, the fractional precipitation method can also be advantageously applied to the separation of soybean saponin, as it utilizes the difference in solubility in organic solvents between soybean saponin and other substances. That is, raw materials containing soybean saponin and other substances are dissolved in a solvent in which they can be dissolved, and this solution is gradually added to a solvent in which one of them is more difficult to dissolve. The final fraction containing the precipitated soybean saponin is collected and the fraction containing other substances is removed. This operation may be repeated with the same solvent system, but it is also possible to select different solvent systems and combine them to make the separation of soybean saponins more effective.
この方法のための溶剤系としては、前記の分配
抽出法においてあげた溶剤の中から選ばれる2種
以上の溶剤から成る相互に混合可能な溶剤系が好
ましい。その例としては、メタノールと酢酸エチ
ル、メタノールもしくは高濃度の水性エタノール
とアセトン等の組み合わせがあげられる。 The solvent system for this method is preferably a mutually miscible solvent system consisting of two or more solvents selected from among the solvents listed in the above-mentioned partition extraction method. Examples include combinations of methanol and ethyl acetate, methanol or highly concentrated aqueous ethanol and acetone.
クロマトグラフイも大豆サポニンの有効な分離
手段である。この場合は大豆サポニン及び他の物
質の混合物である出発原料の処理物を、それらが
可溶の有機溶剤又は混合溶剤、例えばメタノール
単独、あるいはメタノールと水、クロロホルム、
メタノール及び水の混合溶剤に溶解し、大豆サポ
ニン及び他の物質を吸着もしくは分配可能の充填
物、例えばシリカゲル、化学結合型シリカゲル、
粒状活性炭、アルミナ等を予め柱状に充填したカ
ラムを通過させ、大豆サポニン又は他の物質を吸
着させる。 Chromatography is also an effective means of separating soybean saponins. In this case, the treated starting materials, which are mixtures of soybean saponin and other substances, are mixed with organic solvents or mixed solvents in which they are soluble, such as methanol alone, methanol and water, chloroform,
Fillers that are soluble in a mixed solvent of methanol and water and capable of adsorbing or distributing soybean saponin and other substances, such as silica gel, chemically bonded silica gel,
It is passed through a column filled with granular activated carbon, alumina, etc. in advance to adsorb soybean saponin or other substances.
大豆サポニンを吸着させた場合には、更に同系
列で混合割合を変えた有機溶剤、あるいは異系列
で大豆サポニンを溶出し易い有機溶剤で展開し
て、大豆サポニンを溶出させる。大豆サポニン以
外の物質を吸着させた場合は、大豆サポニンは通
過液として得られる。これら溶液中の大豆サポニ
ンは減圧濃縮により有機溶剤を回収することによ
つて採取することができる。なお逆相型の化学結
合型シリカゲル、例えばマイクロボンダパツク
C8又はC18(ウオーターズ社製)及びこれと類似
の充填剤は、目的とする大豆サポニンの精製に好
適である。 When soybean saponin is adsorbed, the soybean saponin is further eluted by developing with the same series of organic solvents with different mixing ratios or with a different series of organic solvents that easily elute soybean saponin. When substances other than soybean saponin are adsorbed, soybean saponin is obtained as a permeate. The soybean saponin in these solutions can be collected by recovering the organic solvent by concentration under reduced pressure. In addition, reverse-phase chemically bonded silica gel, such as Micro Bonder Pack
C8 or C18 (manufactured by Waters) and similar fillers are suitable for purification of the target soybean saponin.
さらに前記の分離手段を適宜組み合わせること
により、良好な結果を得ることができる。 Furthermore, good results can be obtained by appropriately combining the above separation means.
こうして分離された大豆サポニンは、そのまま
製品としてもよいが、必要により更にこれを水性
低級アルコール例えば水性メタノール、水性エタ
ノール等を用いて再結晶することにより、、高純
度の大豆サポニンとすることができる。 The soybean saponin thus separated may be used as a product as it is, but if necessary, it can be further recrystallized using an aqueous lower alcohol such as aqueous methanol, aqueous ethanol, etc. to obtain highly purified soybean saponin. .
本発明は、利用価値の低い醤油粕から有用な大
豆サポニンを安価に提供しうる点で、工業的価値
のきわめて大きいものである。 The present invention has extremely great industrial value in that useful soybean saponin can be provided at low cost from soy sauce lees, which has low utility value.
実施例 1
濃口醸造醤油粕を粉砕機にかけて粉末となし、
その400gを2容の丸底フラスコに入れ、これ
に酢酸エチル1を加えて5時間還流加熱する。
次いで過により酢酸エチル抽出液を除き、残査
について同様の酢酸エチル抽出を合計で5回行
う。Example 1 Koikuchi brewed soy sauce lees was crushed into powder,
400 g of the mixture was placed in a 2-volume round bottom flask, 1 portion of ethyl acetate was added thereto, and the mixture was heated under reflux for 5 hours.
Then, the ethyl acetate extract is removed by filtration, and the residue is subjected to the same ethyl acetate extraction five times in total.
こうして得られた脱脂醤油粕を2容の丸底フ
ラスコに採り、これにメタノール1を加えて5
時間加熱還流する。次いで過してメタノール抽
出液を採取し、残査について同様のメタノール抽
出を合計で3回行う。これらのメタノール抽出液
を合わせ、減圧で溶剤を留去すると、メタノール
抽出エキス65gが得られる。 The defatted soy sauce lees obtained in this way was taken into a 2-volume round bottom flask, and 1 volume of methanol was added to it.
Heat to reflux for an hour. Then, the methanol extract is collected by filtration, and the residue is subjected to the same methanol extraction three times in total. These methanol extracts are combined and the solvent is distilled off under reduced pressure to obtain 65 g of methanol extract.
このメタノール抽出エキス65gをn−ブタノー
ル300mlと水300mlで分配し、n−ブタノールへ移
行した区分の溶剤を留去すると、19gのエキスが
得られる。 65 g of this methanol extracted extract is distributed between 300 ml of n-butanol and 300 ml of water, and the solvent transferred to n-butanol is distilled off to obtain 19 g of extract.
このエキス19gをメタノール30mlに溶解し、こ
れを酢酸エチル1.5中に滴加し、生じた沈殿を
遠心分離して集めると、沈殿物6gが得られる。 Dissolve 19 g of this extract in 30 ml of methanol, add dropwise to 1.5 mL of ethyl acetate, and collect the resulting precipitate by centrifugation to obtain 6 g of precipitate.
この沈殿物6gをメタノール300mlに溶解し、
活性炭20gを加えて12時間撹拌する。次いで活性
炭を過により除去し、液を減圧濃縮すると、
粗大豆サポニン分画2gが得られる。 Dissolve 6g of this precipitate in 300ml of methanol,
Add 20g of activated carbon and stir for 12 hours. Then, the activated carbon was removed by filtration, and the liquid was concentrated under reduced pressure.
2 g of crude soybean saponin fraction is obtained.
粗大豆サポニン分画2gをメタノール500mlに
溶解し、1容の丸底フラスコに入れ、これに5
%苛性カリ−メタノール溶液20mlを加え、1時間
還流加熱したのち、強酸性イオン交換樹脂で中和
する。次いで過により樹脂を除去し、液を減
圧で溶剤を留去する。こうして得られた1.8gの
残査を逆相シリカゲルカラムクロマトグラフイ
〔担体:ボンダパツクC18(ウオーターズ社製)
100g、溶媒:メタノール−水(1:2〜1:
1)〕で精製すると、大豆サポニンが1.5g得られ
る。 Dissolve 2 g of the crude soybean saponin fraction in 500 ml of methanol, put it in a 1 volume round bottom flask, and add 5
After adding 20 ml of % caustic potash methanol solution and heating under reflux for 1 hour, the mixture was neutralized with a strongly acidic ion exchange resin. Then, the resin is removed by filtration, and the solvent is distilled off from the liquid under reduced pressure. 1.8 g of the residue thus obtained was subjected to reverse phase silica gel column chromatography [Carrier: Bondapak C18 (manufactured by Waters)]
100g, solvent: methanol-water (1:2-1:
1)] yields 1.5g of soybean saponin.
この大豆サポニンをシリカゲルを用いた薄層ク
ロマトグラフイ〔プレコートのシリカゲル
60F254、層の厚さ0.25mm(メルク社製)、展開溶
媒:クロロホルム−メタノール−水(65:35:10
の下層〜6:4:1)〕に付し、50%硫酸溶液を
噴霧したのち90〜95℃に5分間加熱すると、顕著
に検出されるスポツトとして、Rf値が0.26、
0.30、0.34及び0.37のいずれも大豆サポニンに特
有の赤紫色のスポツトが得られる。これは例えば
ジヤーナル・オブ・ザ・アメリカン・オイル・ケ
ミスツ・ソサエテイ47巻3号86〜90頁(1970年)
に記載の大豆サポニンの薄層クロマトグラフイの
結果によく一致し、前記のようにして得られたサ
ポニンが大豆サポニンであることが確認される。 This soybean saponin was analyzed by thin layer chromatography using silica gel [pre-coated silica gel].
60F254, layer thickness 0.25 mm (manufactured by Merck), developing solvent: chloroform-methanol-water (65:35:10)
When sprayed with 50% sulfuric acid solution and heated to 90-95℃ for 5 minutes, spots with an Rf value of 0.26,
For all of 0.30, 0.34 and 0.37, reddish-purple spots characteristic of soybean saponin are obtained. For example, Journal of the American Oil Chemistry Society, Vol. 47, No. 3, pp. 86-90 (1970)
This result agrees well with the thin layer chromatography results for soybean saponin described in 2009, confirming that the saponin obtained as described above is soybean saponin.
実施例 2
濃口醸造醤油粕をクラツシヤーにかけてフレー
ク状となし、その2Kgを20容のほうろうタンク
に入れ、これに80%V/V水性エタノール12を
加えて蓋を閉じ、室温で一夜浸漬抽出する。この
抽出液を通常の傾斜法によつて採取し、残査につ
いて同様の水性エタノール抽出を合計で2回行
う。水性エタノール抽出液を合わせ、過して得
られた清澄液をフラツシユエバポレーターにより
減圧下に全量が約1.2になるまで濃縮する。Example 2 Koikuchi brewed soy sauce lees is crushed into flakes, 2 kg of which is put into a 20-volume enamel tank, 12 parts of 80% V/V aqueous ethanol is added thereto, the lid is closed, and immersion extraction is carried out overnight at room temperature. This extract is collected by a conventional decanting method, and the residue is subjected to a total of two similar aqueous ethanol extractions. The aqueous ethanol extracts are combined and filtered, and the resulting clear liquid is concentrated under reduced pressure using a flash evaporator until the total volume is approximately 1.2.
濃縮液を直径60cm、高さ50cmの液体クロマト用
カラムに入れ、一夜静置する。その際濃縮液は2
層に分離するので、その下層をカラムの下部より
取り出し、珪藻土を助剤として過することによ
り、なお若干混在する脂質を除去すると、清澄液
が1得られる。この清澄液から溶剤をフラツシ
ユエバポレーターにより減圧下に留去すると、エ
キスが230g得られる。 Pour the concentrated solution into a liquid chromatography column with a diameter of 60 cm and a height of 50 cm, and leave it overnight. At that time, the concentrate is 2
Since it is separated into layers, the lower layer is taken out from the bottom of the column and filtered through diatomaceous earth as an auxiliary agent to remove some remaining lipids, yielding a clear liquid. The solvent is distilled off from this clear liquid using a flash evaporator under reduced pressure to obtain 230 g of extract.
このエキス230gにメタノール1を加え、約
70℃に加熱してエキスをできるだけ溶解し、冷却
して放置する。生成した沈殿物を過により除去
し、液を同様に減圧下に濃縮乾固すると、メタ
ノール可溶エキスが160g得られる。このエキス
160gをn−ブタノール400mlと水600mlで分配し、
n−ブタノールへ移行した区分の溶剤を留去する
と、エキスが42g得られる。 Add 1 part methanol to 230g of this extract, and add approximately
Heat to 70℃ to dissolve as much of the extract as possible, then cool and leave. The formed precipitate was removed by filtration, and the liquid was similarly concentrated to dryness under reduced pressure to obtain 160 g of methanol-soluble extract. This extract
Distribute 160 g with 400 ml of n-butanol and 600 ml of water,
When the solvent in the portion transferred to n-butanol is distilled off, 42 g of extract is obtained.
このエキス42gをメタノール60mlに溶解し、こ
れをアセトン1.2中に滴加し、生じた沈殿を遠
心分離して集める(収量24g)。この沈殿物24g
をメタノール1.2に溶解し、これに活性炭40g
を加えて12時間撹拌する。この溶液より活性炭を
過により除去し、液から溶剤を留去すると、
粗大豆サポニン分画が10g得られる。 Dissolve 42 g of this extract in 60 ml of methanol, add dropwise to 1.2 g of acetone, and collect the resulting precipitate by centrifugation (yield: 24 g). 24g of this sediment
Dissolve in 1.2 methanol and add 40 g of activated carbon to this.
Add and stir for 12 hours. Activated carbon is removed from this solution by filtration, and the solvent is distilled off from the solution.
10 g of crude soybean saponin fraction is obtained.
この粗大豆サポニン分画10gを実施例1と同様
の方法で更に精製すると、目的の大豆サポニンが
7.2g得られる。 When 10 g of this crude soybean saponin fraction was further purified in the same manner as in Example 1, the desired soybean saponin was obtained.
7.2g obtained.
実施例 3
淡口醸造醤油粕2Kgを実施例2の方法で処理し
て得られた、水性エタノール抽出液の濃縮分離液
の下層1に、水200mlを添加し、アルコール濃
度を30%V/Vに調整したのち、珪藻土を用いる
過により懸濁物を除去すると、清澄液が1.2
得られる。Example 3 200 ml of water was added to the lower layer 1 of the concentrated separation liquid of the aqueous ethanol extract obtained by processing 2 kg of Usukuchijozo soy sauce lees by the method of Example 2, and the alcohol concentration was adjusted to 30% V/V. After adjustment, the suspended matter is removed by filtration using diatomaceous earth, and the clear liquid has a concentration of 1.2
can get.
この清澄液1.2をスチレン系吸着樹脂アンバ
ーライトXAD−2(ロームアンドハース社製)の
カラム(直径6cm×高さ50cm)にSV=1の流速
で通過させ、30%V/V水性エタノール400mlで
洗浄したのち、吸着部をメタノール1で溶出
し、溶出液の溶剤を減圧下に留去すると、エキス
が40g得られる。 This clarified liquid 1.2 was passed through a column (diameter 6 cm x height 50 cm) of styrene adsorption resin Amberlite XAD-2 (manufactured by Rohm and Haas) at a flow rate of SV = 1, and 400 ml of 30% V/V aqueous ethanol After washing, the adsorption area is eluted with 1 part of methanol, and the solvent of the eluate is distilled off under reduced pressure to obtain 40 g of extract.
このエキス40gをメタノール60mlに溶解し、こ
れをアセトン1.2中に滴加し、生じた沈殿を遠
心分離して集めると、沈殿物が20g得られる。以
下実施例2と同様にして活性炭処理を施し、更に
実施例1と同様にして精製処理すると、目的の大
豆サポニンが7.4g得られる。 Dissolve 40 g of this extract in 60 ml of methanol, add dropwise to 1.2 mL of acetone, and collect the resulting precipitate by centrifugation to obtain 20 g of the precipitate. Thereafter, activated carbon treatment was performed in the same manner as in Example 2, and further purification treatment was performed in the same manner as in Example 1, to obtain 7.4 g of the desired soybean saponin.
Claims (1)
れる脱脂醤油粕に、水及び/又は低級アルコール
を加えて抽出し、得られた抽出部に、有機溶剤に
よる分配抽出、非イオン性吸着樹脂による吸着脱
離、分別沈殿及びクロマトグラフイより選ばれた
少なくとも1種の分離手段を施して大豆サポニン
を分離することを特徴とする、大豆サポニンの製
造法。 Soy sauce lees or defatted soy sauce lees obtained by degreasing this with an organic solvent is extracted by adding water and/or lower alcohol, and the resulting extraction part is subjected to partition extraction with an organic solvent and nonionic adsorption resin. A method for producing soybean saponin, which comprises separating soybean saponin by applying at least one type of separation means selected from adsorption/desorption, fractional precipitation, and chromatography.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57117854A JPS5910520A (en) | 1982-07-08 | 1982-07-08 | Production of soybean saponin |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57117854A JPS5910520A (en) | 1982-07-08 | 1982-07-08 | Production of soybean saponin |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5910520A JPS5910520A (en) | 1984-01-20 |
JPH0352447B2 true JPH0352447B2 (en) | 1991-08-12 |
Family
ID=14721928
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57117854A Granted JPS5910520A (en) | 1982-07-08 | 1982-07-08 | Production of soybean saponin |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5910520A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011116679A (en) * | 2009-12-01 | 2011-06-16 | Ishikawa Prefecture | Bile acid adsorbent |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59137421A (en) * | 1983-01-28 | 1984-08-07 | Naganoken Kooridoufu Kogyo Kyodo Kumiai | Preparation of physiologically active substance |
JPS617286A (en) * | 1984-06-22 | 1986-01-13 | Kishimoto Sangyo Kk | Production of isolated saponin |
JPS617285A (en) * | 1984-06-22 | 1986-01-13 | Kishimoto Sangyo Kk | Extraction of purified saponin |
KR20060039379A (en) * | 2004-11-02 | 2006-05-08 | 신경철 | Method of preparing lumen extract for cosmetic composition |
JP2011195541A (en) * | 2010-03-23 | 2011-10-06 | Fuji Oil Co Ltd | Method for producing group b saponin |
CN102702273A (en) * | 2012-05-24 | 2012-10-03 | 福建农林大学 | Extraction method of lotus seed oligosaccharide |
CN103408614A (en) * | 2013-07-31 | 2013-11-27 | 李玉山 | Novel preparation technique of steviosin and Rebaudioside-A |
-
1982
- 1982-07-08 JP JP57117854A patent/JPS5910520A/en active Granted
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011116679A (en) * | 2009-12-01 | 2011-06-16 | Ishikawa Prefecture | Bile acid adsorbent |
Also Published As
Publication number | Publication date |
---|---|
JPS5910520A (en) | 1984-01-20 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US6989098B2 (en) | Methods for the isolation, recovery and purification of non-polar compounds using novel hydrophobically-modified polysaccharide gels | |
CN104086425A (en) | Method for simultaneously extracting and separating chlorogenic acid, solanesol, alkaloid and rutin in tobacco | |
CN106749448B (en) | A kind of method that Simulated Moving Bed Chromatography method extracts steviol glycoside in STEVIA REBAUDIANA | |
JP2009120494A (en) | Method for producing fucoxanthin-rich brown algae extract | |
CN112266399B (en) | High-purity separation and extraction method of epimedium extract | |
JPH0352447B2 (en) | ||
CN107778277B (en) | Process for the recovery of squalene, vitamin E and/or sterols | |
EP1341801B1 (en) | A process for isolating saponins from soybean-derived materials | |
US20220234981A1 (en) | Extraction and purification of natural ferulate and coumarate from biomass | |
CN104418740B (en) | The method of high-purity chlorogenic acid is prepared from leaf of canada potato | |
CN102924537B (en) | Method for preparing hyperoside and isoquercitrin simultaneously from dogbane leaves | |
JPS617285A (en) | Extraction of purified saponin | |
CN101160160B (en) | A process for the isolation of pharmacologically active principles of vegetable and animal origin | |
JPS59175496A (en) | Isolation of soyasaponin | |
CN102702286A (en) | Method for separating and purifying aucubin from leaves of eucommia ulmoides oliv with NKA-2 macroporous adsorption resin | |
CN113336755A (en) | Method for separating and purifying trigonelline, chlorogenic acid and caffeine | |
JPS625917A (en) | Production of saponin containing no isoflavone from soybean embro bud | |
Prapakornwiriya et al. | Recovery of sinapic acid from the waste effluent of mustard protein isolation by ion exchange chromatography | |
CN113061156B (en) | A kind of preparation method of vanilla saponin A | |
JP2003171393A (en) | Method for producing high-purity soybean saponin | |
RU2349331C1 (en) | Method of obtaining dihydroquercetin | |
JPS6259116B2 (en) | ||
JPH0684385B2 (en) | Extraction method of saponins | |
JPS6165895A (en) | Novel quassinoid compound and its production | |
CN106866601A (en) | A kind of preparation method of the peaceful B bulk drugs of the root of langdu |