JP2534043B2 - Method for separating active ingredients from cruciferous plants - Google Patents
Method for separating active ingredients from cruciferous plantsInfo
- Publication number
- JP2534043B2 JP2534043B2 JP61233751A JP23375186A JP2534043B2 JP 2534043 B2 JP2534043 B2 JP 2534043B2 JP 61233751 A JP61233751 A JP 61233751A JP 23375186 A JP23375186 A JP 23375186A JP 2534043 B2 JP2534043 B2 JP 2534043B2
- Authority
- JP
- Japan
- Prior art keywords
- extraction
- tank
- carbon dioxide
- component
- peroxidase
- 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
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/54—Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids
Landscapes
- Enzymes And Modification Thereof (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は西洋わさび、大根等の十字花科植物から該植
物中に含有される辛味成分および活性パーオキシダーゼ
の有効成分を分離回収する方法に係り、特にこれら有効
成分を同時に、かつ、それぞれ別々に抽出回収できる十
字花科植物から有効成分の分離方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to a method for separating and recovering from the cruciferous plants such as horseradish and radish, the pungency component and the active component of active peroxidase contained in the plant. In particular, the present invention relates to a method for separating an active ingredient from a crucifer plant capable of extracting and collecting these active ingredients simultaneously and separately.
西洋わさび、大根等の十字花科植物には主として内在
基質チオ配糖体(シニグリン)および内在チオグリコシ
ダーゼ(酵素ミロシナーゼ)、パーオキシダーゼ等が含
有されている。Cruciferous plants such as horseradish and radish mainly contain an endogenous substrate thioglycoside (sinigrin), an endogenous thioglycosidase (enzyme myrosinase), peroxidase and the like.
シニグリンは通常、水および酵素ミロシナーゼの存在
下酵素反応を起こして辛味成分であるアリルイソチオシ
アネートを生成し、香辛成分として利用されている。ま
た、パーオキシダーゼは例えば臨床検査試薬としてグル
コース、コレステロール、リン脂質あるいは尿酸の定量
に利用され、さらには食品分析用試薬としても広く利用
されており、これらはいずれも十字花科植物、例えば西
洋わさびから抽出分離されている。Sinigrin is usually used as a spice ingredient by causing an enzymatic reaction in the presence of water and the enzyme myrosinase to produce an allyl isothiocyanate which is a spicy ingredient. Further, peroxidase is used, for example, as a clinical test reagent for the determination of glucose, cholesterol, phospholipids or uric acid, and is also widely used as a reagent for food analysis, and these are all cruciferous plants such as horseradish. Has been extracted and separated from.
前述の有効成分である辛味成分およびパーオキシダー
ゼは従来、それぞれ別々に抽出分離されていた。すなわ
ち、辛味成分は例えば西洋わさびをすりおろし、酵素反
応を起こしたのち、約110℃の温度で水蒸気蒸溜して抽
出分離され、また、パーオキシダーゼはこれとは別に西
洋わさびをすりおろし、食塩水中に撹拌しながら浸漬し
て抽出分離されていた。Conventionally, the above-mentioned active ingredients, the pungent ingredient and peroxidase, have conventionally been separately extracted and separated. That is, for example, the spicy ingredient is grated with horseradish, which undergoes an enzymatic reaction and is then extracted and separated by steam distillation at a temperature of about 110 ° C. Peroxidase is grated with horseradish separately and then in saline. The solution was extracted and separated by immersing in agitating.
しかし、前述の辛味成分の抽出分離ではパーオキシダ
ーゼは高温のために失活してしまい、パーオキシダーゼ
の抽出分離では辛味成分は回収されずに揮散あるいは変
質してしまい、このため、辛味成分とパーオキシダーゼ
の同時抽出回収が強く望まれていた。However, in the above-mentioned extraction and separation of the pungency component, peroxidase is inactivated due to the high temperature, and in the extraction and separation of peroxidase, the pungency component is volatilized or deteriorated without being recovered. The simultaneous extraction and recovery of oxidase has been strongly desired.
本発明の目的は辛味成分とパーオキシダーゼを同時に
抽出回収し得る、前述の従来技術の欠点を改良した十字
花科植物から有効成分の分離方法を提供することにあ
る。An object of the present invention is to provide a method for separating an active ingredient from a cruciferous plant, which is capable of simultaneously extracting and recovering a pungent ingredient and peroxidase, and which has improved the above-mentioned drawbacks of the prior art.
前述の目的を達成するため、本発明によれば、原料と
しての十字花科植物を抽出槽中で酵素反応を起こして辛
味成分を生成せしめるとともに、この槽中に超臨界二酸
化炭素または液化炭酸を導入して前記辛味成分を前記超
臨界二酸化炭素または液化炭酸中に抽出し、次いで前記
辛味成分を含有した超臨界二酸化炭素または液化炭酸を
分離槽に導入して前記辛味成分を分離回収し、さらに前
記抽出槽中の残査から活性パーオキシダーゼを分離回収
して前記十字花科植物中に含有される辛味成分および活
性パーオキシダーゼの有効成分を同時に、それぞれ分離
回収することを特徴とする。In order to achieve the above-mentioned object, according to the present invention, a cruciferous plant as a raw material is subjected to an enzymatic reaction in an extraction tank to generate a pungency component, and supercritical carbon dioxide or liquefied carbonic acid is added to this tank. Introducing and extracting the pungent component into the supercritical carbon dioxide or liquefied carbonic acid, then introducing supercritical carbon dioxide or liquefied carbonic acid containing the pungent component into a separation tank to separate and recover the pungent component, The active peroxidase is separated and recovered from the residue in the extraction tank, and the pungency component and the active component of the active peroxidase contained in the cruciferous plant are separately collected at the same time.
以下、本発明を添付図面を用い、かつ十字花科植物と
して西洋わさびを用いて詳述する。Hereinafter, the present invention will be described in detail with reference to the accompanying drawings and using horseradish as a crucifer.
まず、生西洋わさびを冷却槽1に投入して凍結点以下
の低温で凍結し、次いで粉砕機2でこの凍結状態を維持
しながら凍結粉砕する。冷却槽1の冷媒は液体窒素等で
ある。また、粉砕機2は通常の粉砕機、あるいはおろし
がね等である。First, raw horseradish is put into the cooling tank 1 and frozen at a low temperature below the freezing point, and then freeze-pulverized by the pulverizer 2 while maintaining this frozen state. The coolant in the cooling tank 1 is liquid nitrogen or the like. The crusher 2 is an ordinary crusher or a grater.
次いで、粉砕機2によって粉砕化された凍結物を抽出
槽3に充填して加温し、酵素反応を起こして辛味成分
(アリルイソチオシアネート)を生成する。原料として
乾燥西洋わさびを用いた場合には抽出槽3内にエントレ
ーナ装置により水を導入して水分が10%以上、好ましく
は30乃至50%(いずれも重量)になるように調節して酵
素反応を起こす。また、常温粉砕あるいは常温すりおろ
しの場合にはそのままの状態で酵素反応を起こす。Next, the frozen substance pulverized by the pulverizer 2 is filled in the extraction tank 3 and heated to cause an enzymatic reaction to generate a pungency component (allyl isothiocyanate). When dry horseradish is used as the raw material, water is introduced into the extraction tank 3 by an entrainer device and the water content is adjusted to 10% or more, preferably 30 to 50% (both by weight) to carry out an enzymatic reaction. Cause Further, in the case of crushing at room temperature or grazing at room temperature, the enzyme reaction is caused as it is.
さらに、前述の酵素反応と同時に抽出槽3中に超臨界
二酸化炭素または液化炭酸の溶媒を導入して、前記酵素
反応によって生成された辛味成分をこれら超臨界二酸化
炭素または液化炭酸の溶媒に抽出する。前記導入に際し
て、超臨界二酸化炭素の場合には温度30℃以上、圧力75
気圧以上の条件下で導入され、また、液化炭酸の場合に
は例えば温度20℃、圧力200気圧の条件下で導入され
る。Furthermore, a solvent of supercritical carbon dioxide or liquefied carbonic acid is introduced into the extraction tank 3 at the same time as the above-mentioned enzymatic reaction, and the pungent component produced by the enzyme reaction is extracted into the solvent of supercritical carbon dioxide or liquefied carbonic acid. . At the time of the introduction, in the case of supercritical carbon dioxide, a temperature of 30 ° C or higher, a pressure of 75
It is introduced under atmospheric pressure or higher, and in the case of liquefied carbonic acid, for example, the temperature is 20 ° C. and the pressure is 200 atmospheric pressure.
このようにして得られた辛味成分の含有された溶媒は
分離槽4に導入され、減圧されてガス相ならびに液相に
相分離され、分離槽4からガスとして放出されて有用物
質である辛味成分のみが選択的に分離回収される。The solvent containing the pungency component thus obtained is introduced into the separation tank 4, decompressed and phase-separated into a gas phase and a liquid phase, and released from the separation tank 4 as a gas, which is a useful substance. Only the separated and recovered.
さらに、本発明では抽出槽3に残存している残査から
通常の方法でパーオキシダーゼを抽出分離する。Further, in the present invention, peroxidase is extracted and separated from the residue remaining in the extraction tank 3 by a usual method.
本発明は抽出溶媒として超臨界二酸化炭素または液化
炭酸を用いるため、抽出槽3における残査中のパーオキ
シダーゼは死滅せずに残存し、これを残査から回収する
ことにより辛味成分とパーオキシダーゼの同時抽出回収
が可能となる。Since supercritical carbon dioxide or liquefied carbonic acid is used as the extraction solvent in the present invention, the peroxidase in the residue in the extraction tank 3 remains without being killed, and by recovering this from the residue, the pungency component and the peroxidase are separated. Simultaneous extraction and collection becomes possible.
実施例 1 生西洋わさび100kg(水分含有量約70%)を常温です
りおろして抽出槽に充填した。この抽出槽内温度を40℃
に保ち、40℃、200気圧の超臨界二酸化炭素を導入し、
撹拌しながら約2時間抽出を行った。次いで、この超臨
界二酸化炭素を減圧弁を通して分離槽に導き、50気圧に
減圧して超臨界二酸化炭素を炭酸ガスとして放出し、辛
味成分としてのアリルイソチオシアネート0.3kgを得
た。Example 1 100 kg of fresh horseradish (water content about 70%) was grated at room temperature and filled in an extraction tank. The temperature inside this extraction tank is 40 ℃
Kept at 40 ° C and 200 atm of supercritical carbon dioxide was introduced,
Extraction was performed for about 2 hours with stirring. Next, this supercritical carbon dioxide was introduced into a separation tank through a pressure reducing valve, and was depressurized to 50 atm to release supercritical carbon dioxide as carbon dioxide gas to obtain 0.3 kg of allyl isothiocyanate as a pungency component.
次いで、抽出槽内に残存したペースト状の西洋わさび
残査を別の抽出槽に移し、パーオキシダーゼを抽出分離
した。この抽出分離は次の方法により行った。Then, the paste-like horseradish residue remaining in the extraction tank was transferred to another extraction tank, and peroxidase was extracted and separated. This extraction separation was performed by the following method.
抽出残査に水を140加え、よく撹拌し、一夜放置後
エタノール、クロロホルム(2:1)混液54を加えて0
℃で20分撹拌し、遠心分離(3,000rpm15分間)して上澄
液を得る。次いで、2Nカセイソーダで5.5とし、30℃以
下で減圧濃縮して40にする。これに硫安を添加(250g
/)し、生ずる沈澱を遠沈除去する。上澄液にさらに
硫安を添加(250g/)し、生じた沈澱を遠沈して集め
る。この沈澱を0.2Mリン酸緩衝液(PH7)1に懸濁
し、一夜透析する。沈澱を遠沈除去して、上澄液を得
る。これを冷却して1.5倍容のエタノールを加え、生ず
る沈澱を集める。これを水に溶解してアルコール分別沈
澱により精製する。すなわち、1回目はエタノール添加
(1.2〜2.0容)で沈澱する区分を集め、これを水に溶解
して再びエタノール添加(1.3〜1.9容)で沈澱する区分
を集める。これを1の水にとかし、硫安を加えてその
飽和度が0.56〜0.70で沈澱する区分をとり、少量の水に
溶解し、硫安飽和液を滴下して、わずかな混濁を生ぜし
めた後、冷却して結晶種を添加し、室温に放置すれば数
時間で結晶が析出し、パーオキシダーゼを得た。To the extraction residue, add 140 water, stir well, let stand overnight, add a mixture of ethanol and chloroform (2: 1) 54, and add 0.
Stir for 20 minutes at ℃ and centrifuge (3,000 rpm for 15 minutes) to obtain a supernatant. Then, it is adjusted to 5.5 with 2N sodium hydroxide and concentrated under reduced pressure at 30 ° C or lower to 40. Ammonium sulfate was added to this (250 g
/) And remove the resulting precipitate by centrifugation. Ammonium sulfate was further added to the supernatant (250 g /), and the resulting precipitate was collected by centrifugation. The precipitate is suspended in 0.2M phosphate buffer (PH7) 1 and dialyzed overnight. The precipitate is removed by centrifugation to obtain a supernatant. It is cooled and 1.5 volumes of ethanol are added and the resulting precipitate is collected. This is dissolved in water and purified by alcoholic precipitation. That is, at the first time, the sections that precipitate by the addition of ethanol (1.2 to 2.0 volumes) are collected, and the sections that dissolve in water and precipitate again by the addition of ethanol (1.3 to 1.9 volumes) are collected. Dissolve this in water 1 and add ammonium sulphate to take a section where the degree of saturation precipitates at 0.56 to 0.70. Dissolve in a small amount of water and add ammonium sulphate saturated solution dropwise to give a slight turbidity. When cooled and added with crystal seeds and left at room temperature, crystals were precipitated in several hours to obtain peroxidase.
実施例 2 西洋わさび100kgを実施例1と同様にしてすりおろ
し、抽出槽に充填した。この抽出槽内温度を20℃に保
ち、20℃、200気圧の液化炭酸を導入し、撹拌しながら
2時間抽出を行った。次いで、この液化炭酸を減圧弁を
通して分離槽に導き、50気圧に減圧して液化炭酸を炭酸
ガスとして放出し、辛味成分としてのアリルイソチオシ
アネート0.32kgを得た。Example 2 100 kg of horseradish was grated in the same manner as in Example 1 and filled in an extraction tank. The temperature in this extraction tank was kept at 20 ° C., liquefied carbonic acid at 20 ° C. and 200 atm was introduced, and extraction was carried out for 2 hours while stirring. Next, this liquefied carbonic acid was introduced into a separation tank through a pressure reducing valve, and the pressure was reduced to 50 atm to release the liquefied carbonic acid as carbon dioxide gas to obtain 0.32 kg of allyl isothiocyanate as a pungency component.
次いで、抽出槽内に残存したペースト状の西洋わさび
残査を別の抽出槽に移し、実施例1と同じ方法でパーオ
キシダーゼを抽出分離した。Then, the paste-like horseradish residue remaining in the extraction tank was transferred to another extraction tank, and peroxidase was extracted and separated by the same method as in Example 1.
以上のとおり、本発明は抽出溶媒として超臨界二酸化
炭素または液化炭酸を用いたから、辛味成分およびパー
オキシダーゼの両有効成分を同時に分離回収できる。As described above, since supercritical carbon dioxide or liquefied carbonic acid is used as the extraction solvent in the present invention, it is possible to separate and recover both active ingredients of the pungency component and peroxidase at the same time.
図面は本発明の工程を示したブロック図である。 1……冷却槽、2……粉砕機、3……抽出槽、4……分
離槽。The drawings are block diagrams showing the steps of the present invention. 1 ... Cooling tank, 2 ... Crusher, 3 ... Extraction tank, 4 ... Separation tank.
Claims (1)
素反応を起こして辛味成分を生成せしめるとともに、こ
の槽中に超臨界二酸化炭素または液化炭酸を導入して前
記辛味成分を前記超臨界二酸化炭素または液化炭酸中に
抽出し、次いで前記辛味成分を含有した超臨界二酸化炭
素または液化炭酸を分離槽に導入して前記辛味成分を分
離回収し、さらに前記抽出槽中の残査から活性パーオキ
シダーゼを分離回収して前記十字花科植物中に含有され
る辛味成分および活性パーオキシダーゼの有効成分を同
時に、それぞれ分離回収することを特徴とする十字花科
植物から有効成分の分離方法。1. A cruciferous plant as a raw material is subjected to an enzymatic reaction in an extraction tank to produce a pungent ingredient, and supercritical carbon dioxide or liquefied carbonic acid is introduced into this tank to remove the pungent ingredient from the above-mentioned pungent ingredient. Extraction into critical carbon dioxide or liquefied carbonic acid, then introducing supercritical carbon dioxide or liquefied carbonic acid containing the pungent component into a separation tank to separate and recover the pungent component, and further activate from the residue in the extraction tank A method for separating an active ingredient from a crucifer plant, which comprises separating and collecting peroxidase to simultaneously separate and collect the pungency component and the active component of active peroxidase contained in the crucifer plant.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61233751A JP2534043B2 (en) | 1986-10-01 | 1986-10-01 | Method for separating active ingredients from cruciferous plants |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61233751A JP2534043B2 (en) | 1986-10-01 | 1986-10-01 | Method for separating active ingredients from cruciferous plants |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6387977A JPS6387977A (en) | 1988-04-19 |
JP2534043B2 true JP2534043B2 (en) | 1996-09-11 |
Family
ID=16960005
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61233751A Expired - Lifetime JP2534043B2 (en) | 1986-10-01 | 1986-10-01 | Method for separating active ingredients from cruciferous plants |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2534043B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102871066A (en) * | 2011-07-11 | 2013-01-16 | 浙江科技学院 | Preparation of food-grade natural isorhodanate by application of supercritical CO2 extraction technology |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5928473A (en) * | 1982-08-09 | 1984-02-15 | Toyobo Co Ltd | Preparation of peroxidase |
JPS61129003A (en) * | 1984-11-28 | 1986-06-17 | Hitachi Ltd | Extractive separation apparatus |
JPS61227787A (en) * | 1985-04-02 | 1986-10-09 | Showa Denko Kk | Deodorization of fermentation product |
-
1986
- 1986-10-01 JP JP61233751A patent/JP2534043B2/en not_active Expired - Lifetime
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5928473A (en) * | 1982-08-09 | 1984-02-15 | Toyobo Co Ltd | Preparation of peroxidase |
JPS61129003A (en) * | 1984-11-28 | 1986-06-17 | Hitachi Ltd | Extractive separation apparatus |
JPS61227787A (en) * | 1985-04-02 | 1986-10-09 | Showa Denko Kk | Deodorization of fermentation product |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102871066A (en) * | 2011-07-11 | 2013-01-16 | 浙江科技学院 | Preparation of food-grade natural isorhodanate by application of supercritical CO2 extraction technology |
Also Published As
Publication number | Publication date |
---|---|
JPS6387977A (en) | 1988-04-19 |
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