JP5246990B2 - Method for extracting / collecting antioxidant components contained in plants - Google Patents

Method for extracting / collecting antioxidant components contained in plants Download PDF

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JP5246990B2
JP5246990B2 JP2005166976A JP2005166976A JP5246990B2 JP 5246990 B2 JP5246990 B2 JP 5246990B2 JP 2005166976 A JP2005166976 A JP 2005166976A JP 2005166976 A JP2005166976 A JP 2005166976A JP 5246990 B2 JP5246990 B2 JP 5246990B2
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晃一 中村
賢 和田
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賢 和田
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本発明は、植物の細胞壁に含まれた抗酸化成分を抽出若しくは収集する方法に関する。   The present invention relates to a method for extracting or collecting antioxidant components contained in plant cell walls.

SOD(スーパーオキシドディムスターゼ)は、人体に有害な活性酸素(スーパーオキシドラジカルアニオンO2−)を消去する重要な酵素である。SODは体内で作られ、体内に発生した活性酸素をコントロールする機能を司るが、SODを作りだす機能は、年齢とともに低下し、体内のSODの量が減少すると、皮膚の老化、癌、脳卒中、リュウマチなどのさまざまな障害をもたらすようになってくる。 SOD (superoxide dismutase) is an important enzyme that eliminates active oxygen (superoxide radical anion O 2− ) harmful to the human body. SOD is made in the body and controls the active oxygen generated in the body, but the function to create SOD decreases with age, and when the amount of SOD in the body decreases, skin aging, cancer, stroke, rheumatism It comes to bring various obstacles such as.

このため、食品、体外からSODを摂取する有効な方法としてSOD含有食品あるいは薬品の研究、開発が続けられている。SOD含有食品あるいは薬品の素材として従来から着目されているのが自然植物である。植物は、自身の組織中に活性酸素から組織を守る物質を保有しており、このため、直射日光を浴びることによって、組織内に活性酸素が発生しても、その影響を受けることなく成長することができる。   For this reason, research and development of SOD-containing foods or drugs have been continued as effective methods for taking SOD from foods and outside the body. Conventionally, natural plants have been attracting attention as materials for SOD-containing foods or medicines. Plants have substances in their tissues that protect the tissues from active oxygen, so they can grow without being affected by the generation of active oxygen in the tissues when exposed to direct sunlight. be able to.

特に稲や麦などは生命力が強く、活性酸素を多量に発生させるパラコートなどの除草剤が散布されても枯れることがない。とりわけ、芝は、稲科の植物であることから、稲や麦などと同様に多量の除草剤散布に耐えることができる。このような植物に含まれて活性酸素の除去に有効な働きをする成分は、通常「抗酸化成分」といわれ、活性酸素の除去に関してSODと同じような働きをすることからSOD様作用成分とも言われている。   In particular, rice and wheat have strong vitality and do not wither even when sprayed with a herbicide such as paraquat that generates a large amount of active oxygen. In particular, since turf is a plant of the rice family, it can withstand a large amount of herbicide spraying like rice and wheat. Ingredients that are contained in such plants and that work effectively to remove active oxygen are usually referred to as “antioxidant components”, and they function in the same way as SOD with regard to the removal of active oxygen. It is said.

抗酸化成分としては、たとえば、フラボノイド,カロチン,ビタミンC,B2,タンニン,ポリフェノール類などが知られている。したがって、植物中に含まれたこれら抗酸化成分を有効に抽出できれば、抽出された抗酸化成分を摂取して人体のSODの低下を補い、薬品、食品、化粧品などに活用することができるはずである。   As antioxidant components, for example, flavonoids, carotene, vitamin C, B2, tannin, polyphenols, and the like are known. Therefore, if these antioxidant components contained in the plant can be extracted effectively, the extracted antioxidant components should be consumed to compensate for the decrease in SOD of the human body and used for medicine, food, cosmetics, etc. is there.

従来から植物中に含まれた抗酸化成分を抽出する方法として種々の方法が提案されてきた。たとえば、特許文献1においては、玄米粉、大豆粉、緑茶紛や焙煎した植物種子、胚芽から活性酸素抑制組成物を抽出する従来法を説明した上で、白鶴霊芝の溶媒抽出物が優れた活性酸素消去能を有することを見出したとしてその葉及び枝、茎、根を常温又は加熱した水及び有機溶媒に抽出する方法を開示し、さらに、特許文献2では、白鶴霊芝および緑茶単独の場合に比して白鶴霊芝および緑茶葉それぞれの水及び/または有機溶媒抽出物を有効成分とする活性酸素消去組成物を提案している。   Conventionally, various methods have been proposed as a method for extracting antioxidant components contained in plants. For example, Patent Document 1 describes a conventional method for extracting an active oxygen-suppressing composition from brown rice flour, soybean flour, green tea powder, roasted plant seeds, and germs. And a method for extracting the leaves, branches, stems and roots to room temperature or heated water and an organic solvent as disclosed in Japanese Patent Application Laid-Open No. 2005-318151. Compared with the case of the above, the active oxygen scavenging composition which uses the water and / or organic-solvent extract of each of white crane reishi and green tea leaves as an active ingredient is proposed.

そのほか、しいたけを原料とするもの、金時草を原料とするものなど植物の組織中に含まれる抗酸化成分を抽出する方法は種々知られているが、植物原料中の抗酸化成分を抽出する方法としては、抗酸化成分を液中に溶出させる方法が殆どである。実際に稲や麦などあるいは芝その他の植物に含まれている抗酸化成分は、植物の硬い細胞壁に多く含まれ、多糖類が多数強固につながった高分子構造をしているために水には溶けにくい。   In addition, there are various known methods for extracting antioxidant components contained in plant tissues such as those using shiitake mushrooms and those using kinkoki grass as raw materials, but the antioxidant components in plant materials are extracted. As a method, most are methods of eluting the antioxidant component in the liquid. In fact, many antioxidant components contained in rice, wheat, turf and other plants are contained in the hard cell walls of plants and have a polymer structure in which many polysaccharides are firmly connected. does not melt easily.

もっとも、このような高分子成分であっても細胞壁を細胞サイズ以下に粉砕することによって水に溶けやすくすることは可能であるが、液中に溶出する成分は、植物組織に含まれる抗酸化成分の一部に過ぎず、液中に溶出した抗酸化成分の効用を高めるには、濃縮しなければならない。
特許公開9−143091号公報 特許公開2002−128688号公報 特許第2939206号公報
However, even with such a polymer component, it is possible to make the cell wall easy to dissolve in water by crushing the cell wall to below the cell size, but the component eluted in the liquid is an antioxidant component contained in the plant tissue In order to enhance the utility of the antioxidant component eluted in the liquid, it must be concentrated.
Japanese Patent Publication No. 9-143091 Japanese Patent Publication No. 2002-128688 Japanese Patent No. 2939206

解決しようとする問題点は、たとえ細胞壁を細胞サイズ以下に粉砕しても、水中に溶出する抗酸化成分は、細胞壁に含まれる抗酸化成分の一部にすぎず、そのままでは濃度が薄くて活性酸素消去能には自づから限度があるという点である。   The problem to be solved is that even if the cell wall is crushed to below the cell size, the antioxidant component eluted in the water is only a part of the antioxidant component contained in the cell wall, and its concentration is low and active as it is The oxygen scavenging ability has its own limit.

本発明は、亜臨界水領域の高温高圧の熱水を用いず、密閉した処理チャンバー内で一定時間をかけて加熱した温度の飽和水蒸気圧のもとで植物原料の加水分解処理によって、植物の細胞壁の高分子構造を切断し、細胞壁に含まれる抗酸化成分を開放して、細胞壁の破壊によって取り出された細胞組織液中に効率よく抽出/収集する点を最大の特徴とする。 The present invention does not use high-temperature and high-pressure hot water in the subcritical water region, but hydrolyzes plant materials under saturated steam pressure at a temperature heated for a certain time in a closed treatment chamber. The greatest feature is that the polymer structure of the cell wall is cut, the antioxidant component contained in the cell wall is released, and the cell wall is efficiently extracted / collected into the cell tissue fluid extracted by the destruction of the cell wall.

本発明によれば、植物原料を直接加熱し、植物原料自身が有する水分を蒸発させ、その水蒸気をもって植物原料を加水分解し、加水分解によって植物の細胞壁を破壊し、細胞壁の高分子構造から抗酸化成分を開放させ、開放された抗酸化成分を植物原料から発した細胞内成分を含む水蒸気および処理チャンバー内に生成され植物原料の固形物中に取り込み、その水蒸気を冷却することによって液体および固形物として回収するため、植物の保有水分以上に余分の水分を含まず、したがって抗酸化成分の抽出/収集効率が高い。また、亜臨界水領域の高温高圧熱水を使用しないため、抽出/収集された植物組織内成分の変質がなく、高濃度、高抗酸化消去能を有する抗酸化成分を得ることができる。 According to the present invention, the plant raw material is directly heated to evaporate the water content of the plant raw material itself, hydrolyze the plant raw material with the water vapor, destroy the plant cell wall by hydrolysis, and resist the polymer structure of the cell wall. The oxidized component is released, and the released antioxidant component is taken into the water vapor containing intracellular components emitted from the plant raw material and into the solid material of the plant raw material generated in the processing chamber, and the water vapor is cooled to cool the liquid and solid Since it is recovered as a product, it does not contain excess water beyond the water content of the plant, and therefore the extraction / collection efficiency of the antioxidant component is high. In addition, since high-temperature and high-pressure hot water in the subcritical water region is not used, an antioxidant component having a high concentration and a high antioxidant scavenging ability can be obtained without alteration of the extracted / collected plant tissue components.

亜臨界水領域の熱水を外部から供給することなく植物組織内成分を変質させずに効率よく抗酸化成分を抽出/収集するという目的を、植物原料を攪拌しつつ加熱して、加熱温度の飽和水蒸気圧のもとで植物組織を加水分解し、加水分解によって植物の細胞壁の高分子構造から開放された抗酸化成分を水蒸気および処理チャンバー内固形生成物中に抽出/収集することによって実現した。   The purpose of extracting / collecting antioxidant components efficiently without altering plant tissue components without supplying external hot water in the subcritical water region is to Realized by hydrolyzing plant tissue under saturated water vapor pressure and extracting / collecting antioxidant components released from the macromolecular structure of the plant cell wall into water vapor and solid product in the processing chamber by hydrolysis .

図1は、本発明による植物の細胞壁に含まれた抗酸化成分の抽出/収集方法の実施に使用する抗酸化成分の抽出装置の外観図、図2は装置の概要を略示的に示す構成図である。図2において、抗酸化成分組成物の抽出装置は、処理チャンバー1と、抽出管2と、冷却塔3と、循環ポンプ4との組み合わせからなっている。処理チャンバー1は、内部に投入された植物原料を加熱して加水分解処理を行う釜であり、その外壁には加熱ヒータ5が装備され、処理チャンバー1と、冷却塔3間は、前記抽出管2で接続されている。   FIG. 1 is an external view of an antioxidant component extraction apparatus used for carrying out the method for extracting / collecting antioxidant components contained in the cell wall of a plant according to the present invention, and FIG. 2 schematically shows the outline of the apparatus. FIG. In FIG. 2, the antioxidant component composition extraction apparatus comprises a combination of a processing chamber 1, an extraction pipe 2, a cooling tower 3, and a circulation pump 4. The processing chamber 1 is a kettle that performs hydrolysis treatment by heating the plant raw material introduced therein, and the outer wall thereof is equipped with a heater 5, and the extraction tube is disposed between the processing chamber 1 and the cooling tower 3. 2 are connected.

抽出管2は、処理チャンバー1の下部の蒸気戻り口6と、上部の蒸気送出口7間をつなぐ循環管路であり、冷却塔3は、その管路内に接続され、循環ポンプ4は、冷却塔3の上流側の管路内に接続されたものである。また、処理チャンバー1は、植物原料の投入口8と排出口9とを有し、その内部には、垂直軸を中心に回転しながら槽内に投入された植物原料を攪拌する攪拌羽根10を装備している。   The extraction pipe 2 is a circulation pipe that connects between the lower steam return port 6 of the processing chamber 1 and the upper steam outlet 7, and the cooling tower 3 is connected in the pipe, and the circulation pump 4 is It is connected in the pipe line on the upstream side of the cooling tower 3. Further, the processing chamber 1 has a plant raw material inlet 8 and a discharge port 9, and a stirring blade 10 for stirring the plant raw material introduced into the tank while rotating about a vertical axis is provided therein. Equipped.

冷却塔3は、抽出管2内の空気(蒸気)を冷却する熱交換器であり、循環ポンプ4は、植物原料の加水分解処理後、処理チャンバー1内の水蒸気を冷却塔3に強制送風するものである。   The cooling tower 3 is a heat exchanger that cools the air (steam) in the extraction pipe 2, and the circulation pump 4 forcibly blows the water vapor in the processing chamber 1 to the cooling tower 3 after hydrolysis of the plant raw material. Is.

次に上記抽出装置を用いて植物原料からその細胞壁に含まれる抗酸化成分を抽出する要領を以下に説明する。植物原料には、その細胞壁内に、例えば、フラボノイド,カロチン,ビタミンC,B2,タンニン,ポリフェノールなどの抗酸化成分といわれる物質をできるだけ多く含む植物を選定し、その細胞壁を破壊し、抗酸化成分を細胞壁から開放するとともに、細胞壁の破壊によって取り出された抗酸化成分を細胞組織液を含む水蒸気および加水分解処理によって処理チャンバー内に生成される植物原料の固形物中に取り込ませることによって抽出/収集する。抗酸化成分の抽出/収集は、原料投入処理に続いて加水分解処理、冷却処理を順次行うことによって行う。
図3に本発明による抗酸化成分の抽出/収集方法フローチャートを示す。
Next, a procedure for extracting the antioxidant component contained in the cell wall from the plant raw material using the above extraction apparatus will be described below. For plant raw materials, for example, a plant containing as much as possible an antioxidant component such as flavonoid, carotene, vitamin C, B2, tannin, polyphenol, etc. is selected in the cell wall, the cell wall is destroyed, and the antioxidant component Is extracted from the cell wall, and the antioxidant component extracted by the destruction of the cell wall is extracted / collected by being taken into the solid material of the plant raw material generated in the treatment chamber by the water vapor containing cell tissue fluid and hydrolysis treatment . Extraction / collection of the antioxidant component is performed by sequentially performing a hydrolysis process and a cooling process following the raw material charging process.
FIG. 3 shows a flowchart of an antioxidant component extraction / collection method according to the present invention.

(1)原料投入処理
原料投入処理は、植物原料を処理チャンバー1内に投入し、処理チャンバー1を密閉する処理である(ステップS1)。植物原料には、抗酸化成分(SOD様作用成分)の含有量が高いとして知られている植物を選定する。例えば稲科の芝,高麗芝,ベント芝,稲麦など、とりわけ大麦の若葉などは有効である。
(1) Raw material charging process The raw material charging process is a process in which a plant raw material is charged into the processing chamber 1 and the processing chamber 1 is sealed (step S1). As the plant raw material, a plant known to have a high content of antioxidant components (SOD-like active components) is selected. For example, grasses such as rice grass, ginseng turf, bent turf and rice wheat are particularly effective.

本発明においては原則的に植物原料が保有する水分をそのまま利用して加熱及び加熱に引き続いて冷却処理を行うが、植物原料が保有する水分量が少ない場合には、必要により20%以下の量の水分を加えることができる。   In the present invention, in principle, the moisture contained in the plant material is used as it is, and the cooling treatment is performed following heating and heating. However, if the amount of moisture contained in the plant material is small, an amount of 20% or less is necessary. Of water can be added.

(2)加水分解処理
加水分解処理は、処理チャンバー1内の植物原料を130℃〜150℃の範囲で加熱し、植物原料に含まれる水分を蒸発させ、その水蒸気雰囲気中に植物原料を一定時間曝して植物原料の細胞壁の組織を破壊し、細胞壁に含まれる抗酸化成分を細胞壁の高分子構造から開放し、植物原料から開放された抗酸化成分を植物原料が自ら発した水蒸気中及び細胞壁の組織が破壊された植物原料の固形物に取り込ませる処理である。処理チャンバー1内に植物原料を投入したのち、投入口8を閉じ、タイマーをセットしてヒータ5に通電し、処理チャンバー1内を130℃〜150℃に加熱する(ステップS2)。処理チャンバー1内の圧力は、その加熱温度での飽和水蒸気圧に保たれる。また、一定間隔(例えば2秒)ごとに1回程度攪拌羽根10を回転駆動して処理チャンバー1内の原料を攪拌する。
(2) Hydrolysis treatment In the hydrolysis treatment, the plant raw material in the treatment chamber 1 is heated in the range of 130 ° C to 150 ° C to evaporate water contained in the plant raw material, and the plant raw material is kept in the water vapor atmosphere for a certain period of time. Exposure to destroy the cell wall tissue of the plant material, release the antioxidant component contained in the cell wall from the polymer structure of the cell wall, and the antioxidant component released from the plant material in the water vapor generated by the plant material itself and in the cell wall This is a treatment for incorporating the solid material of the plant material whose tissue has been destroyed . After the plant raw material is charged into the processing chamber 1, the charging port 8 is closed, a timer is set, the heater 5 is energized, and the processing chamber 1 is heated to 130 ° C. to 150 ° C. (step S2). The pressure in the processing chamber 1 is maintained at the saturated water vapor pressure at the heating temperature. Further, the stirring blade 10 is rotationally driven about once every fixed interval (for example, 2 seconds) to stir the raw material in the processing chamber 1.

この状態で一定時間をかけて加熱した温度での飽和水蒸気圧のもと、130℃〜150℃で植物原料を加熱しながら処理チャンバー1内に発生する蒸気の雰囲気中に植物原料を曝し、130℃〜150℃の範囲内の加熱温度での飽和水蒸気を植物原料に作用させて加水分解処理を進行させ、植物原料は、水蒸気の加水分解作用を受けて図4に示したように植物細胞壁を構成するセルロースの高分子構造を破壊され、植物細胞壁および細胞内に含まれる成分を開放して水蒸気および処理チャンバー内固形生成物中に取り込ませる。 Original saturated steam pressure at the temperature heated over a period of time in this state, exposed to plant material in an atmosphere of steam generated in the processing chamber 1 while heating the plant material at 130 ° C. to 150 DEG ° C., 130 Saturated water vapor at a heating temperature in the range of ℃ to 150 ° C. is allowed to act on the plant raw material to proceed with the hydrolysis treatment, and the plant raw material is subjected to the hydrolytic action of water vapor, so that the plant cell wall as shown in FIG. The cellulosic polymer structure is broken, and the plant cell walls and the components contained in the cells are released to be incorporated into water vapor and the solid product in the processing chamber.

加水分解処理によって、植物原料の細胞壁から開放された抗酸化成分を含む水蒸気を処理チャンバー1内に充満させる。植物原料の加水分解が進行して、予め定められた時間経過後、ヒータ5の電源を遮断して加水分解処理を完了する(ステップS3)。   By the hydrolysis treatment, the treatment chamber 1 is filled with water vapor containing an antioxidant component released from the cell wall of the plant raw material. After the hydrolysis of the plant raw material has progressed and a predetermined time has elapsed, the power supply to the heater 5 is shut off to complete the hydrolysis process (step S3).

植物原料の加水分解処理に要する時間は、処理チャンバー1の容量にもよるが、通常は5〜8時間である。つまり密閉された処理チャンバー1内で、130℃〜150℃の温度で加熱したときには、加熱温度での飽和水蒸気圧のもとで数時間のうちに植物原料を加水分解処理することができる。なお、本発明においては、植物原料の加水分解処理によって、植物原料の細胞壁を破壊し、細胞壁に含まれる抗酸化成分を抽出/収集するのが目的であるが、細胞壁の破壊によって同時に細胞内成分は水蒸気中および処理チャンバー内に生成する植物原料の固形物中に抗酸化成分とともに取り出される。細胞内成分は選択された植物原料の種類によって異なるが、液体は通常木・竹酢液といわれる植物の有効成分である。 The time required for the hydrolysis treatment of the plant raw material is usually 5 to 8 hours, although it depends on the capacity of the treatment chamber 1. That is, when heated in a sealed processing chamber 1 at a temperature of 130 ° C. to 150 ° C., the plant raw material can be hydrolyzed within a few hours under a saturated water vapor pressure at the heating temperature. In the present invention, the purpose is to destroy the cell wall of the plant raw material and extract / collect the antioxidant component contained in the cell wall by hydrolysis treatment of the plant raw material. Is taken out together with antioxidant components in water vapor and in the solid material of the plant material produced in the treatment chamber. Intracellular components varies depending on the kind of the selected plant materials, liquid Ru normally active ingredients der plant called a tree-bamboo vinegar.

(3)冷却処理
冷却処理は、加水分解処理後、処理チャンバー1内の水蒸気を冷却して水蒸気および処理チャンバー内に生成した植物原料の固形物中に含まれる抗酸化成分を抽出/収集する処理である。植物原料の加熱終了後、送出側、戻り側の抽出管のバルブV1、V2を開き、循環ポンプ4を起動して処理チャンバー1内の水蒸気を抽出管2内に吸引し、冷却塔3を経由させて一部を凝結させ、乾燥冷却後の水蒸気は再び処理チャンバー1内に戻し、処理チャンバー1内の水蒸気を冷却塔3と処理チャンバー1間で循環させる。冷却塔3内に送り込まれた水蒸気の一部は、冷却されて水蒸気に含まれる抗酸化成分が細胞内成分とともに凝結して抽出され、その成分液が冷却塔3内に貯められる(ステップS4)。
(3) Cooling treatment The cooling treatment is a treatment for extracting / collecting water vapor and antioxidant components contained in the solid material of the plant material generated in the treatment chamber by cooling the water vapor in the treatment chamber 1 after the hydrolysis treatment. It is. After the heating of the plant material is completed, the valves V1 and V2 of the extraction pipes on the delivery side and the return side are opened, the circulation pump 4 is started and water vapor in the processing chamber 1 is sucked into the extraction pipe 2 and passes through the cooling tower 3 The water vapor after drying and cooling is returned to the processing chamber 1 again, and the water vapor in the processing chamber 1 is circulated between the cooling tower 3 and the processing chamber 1. A part of the water vapor sent into the cooling tower 3 is cooled and the antioxidant component contained in the water vapor is condensed and extracted together with the intracellular components, and the component liquid is stored in the cooling tower 3 (step S4). .

処理チャンバー1内の水蒸気は、冷却処理が繰り返されることによって次第に温度・圧力が下がり、処理チャンバー1内が常温、常圧になったことを確認して冷却塔3のドレインを開き、冷却塔3内で抽出された成分液を容器内に回収すると共に処理チャンバー1内に生成した植物原料の固形物を排出口9から排出し、回収する。
(ステップS5)。
The water vapor in the processing chamber 1 gradually decreases in temperature and pressure as the cooling process is repeated, and after confirming that the processing chamber 1 is at room temperature and normal pressure, the drain of the cooling tower 3 is opened. The component liquid extracted in the container is collected in the container, and the solid material of the plant raw material generated in the processing chamber 1 is discharged from the discharge port 9 and collected.
(Step S5).

本発明においては、密閉した処理チャンバー内で一定時間をかけて加熱した温度130℃〜150℃での飽和水蒸気圧のもとで数時間をかけて加水分解処理し、発生する水蒸気中に含まれる抗酸化成分を抽出するものである。抽出液には、細胞内成分が含まれるが、通常は細胞内成分も有効成分であると考えられるので、あえてこれを抗酸化成分から分離除去する必要はないが、もし必要があれば、細胞内成分と、抗酸化成分を分離して回収することできる。 In the present invention, hydrolysis is performed over several hours under a saturated steam pressure at a temperature of 130 ° C. to 150 ° C. heated for a certain time in a closed processing chamber, and is contained in the generated steam. Extracts antioxidant components. Although the extract contains intracellular components, it is usually not considered necessary to separate and remove this from the antioxidant components because the intracellular components are also considered to be effective components. and the inner component, may be recovered by separating the antioxidants.

本発明の方法を380℃、1.0Mpaのような高温、高圧の亜臨界水雰囲気のもとで植物原料の熱分解処理を行う方法と比べれば、当然分解能力は劣るとはいえ、本発明によれば、細胞壁が強い熱分解作用を受けないため、細胞壁の分解とともに抗酸化成分までが分解されることなく有効に抽出することができる。また、本発明においては基本的に植物原料が保有する水分を蒸発させて発生させた水蒸気および処理チャンバー内に生成した植物原料の固形物中から抗酸化成分を抽出/収集するため、成分が薄められることもなく、したがって、あえて濃縮するまでもなく、細胞内成分を含む高濃度の抗酸化成分をきわめて効率よく抽出/収集できる。しかも、従来細胞壁から抗酸化成分の取出しが困難とされていた植物からであっても、容易に抽出することができる。 Although the method of the present invention is naturally inferior to the method of pyrolyzing plant raw materials under a high-temperature, high-pressure subcritical water atmosphere such as 380 ° C. and 1.0 MPa, According to the above, since the cell wall does not receive a strong thermal decomposition action, the antioxidant can be effectively extracted without being decomposed together with the decomposition of the cell wall. In addition, in the present invention, since the antioxidant component is extracted / collected basically from the water vapor generated by evaporating the water held by the plant material and the solid material of the plant material generated in the treatment chamber, the component is diluted. Therefore, high concentration antioxidant components including intracellular components can be extracted / collected very efficiently without being concentrated. Moreover, it can be easily extracted even from plants that have conventionally been difficult to extract antioxidant components from the cell wall.

本発明においては、原料投入処理において、処理チャンバー1内には、植物原料とともに、20%以下の量の水分を投入する場合も含まれる。植物原料に水分を加えると、発生水蒸気量が多くなって、当然抗酸化成分の濃度が低下するが、植物原料に含まれる水分量が少ないときには、水蒸気を発生させるために水分を補うことは必要である。加水分解処理において、植物原料は炭化してはならないし、また、亜臨界水領域となる高温、高圧のもとでは、植物原料の細胞そのものまでが熱分解してしまって、細胞壁から抗酸化成分を有効に抽出できない。   In the present invention, in the raw material charging process, the processing chamber 1 includes a case where a 20% or less amount of water is charged together with the plant raw material. When water is added to plant materials, the amount of water vapor generated increases, naturally reducing the concentration of antioxidant components, but when the amount of water contained in plant materials is small, it is necessary to supplement the water to generate water vapor It is. In the hydrolysis treatment, the plant raw material must not be carbonized, and under high temperature and high pressure in the subcritical water region, the cells of the plant raw material itself are thermally decomposed, and the antioxidant component from the cell wall. Cannot be extracted effectively.

以下に本発明の実験例を示す。
以下にベント芝の葉A,高麗芝の葉と、野芝の葉との混合物B,葉、茎、根を含む高麗芝と野芝との混合物Cを試料として以下の実験を行った。それぞれの試料を細かく粉砕し、その粉砕物を130〜150℃の水蒸気圧を作用させて加水分解処理を行い、冷却後、凝結した抽出液の原液にキサンチン/キサンチンオキシダーゼ(XOD)を0.1ml添加し、XODの添加によって抽出液に生じる電流値の変化を測定した。測定器には、北斗電工株式会社製の活性酸素測定装置(HZ5000)を用いた。
Experimental examples of the present invention are shown below.
The following experiment was carried out using a mixture of Bent turf leaf A, Gano turf leaf and wild turf leaf B, and K turf grass and wild turf mixture C containing leaves, stems and roots as samples. Each sample is finely pulverized, and the pulverized product is hydrolyzed by applying a water vapor pressure of 130 to 150 ° C. After cooling, 0.1 ml of xanthine / xanthine oxidase (XOD) is added to the stock solution of the condensed extract. And the change in the current value generated in the extract by addition of XOD was measured. As a measuring device, an active oxygen measuring device (HZ5000) manufactured by Hokuto Denko Co., Ltd. was used.

測定結果を以下に示す。図5はブランクであり、XOD添加時の活性酸素系の活性酸素生成量について時間的変化を示している。図に明らかなようにXODの添加によって、活性酸素の発生を妨げる物質がなければ、測定開始後、約80秒を経過した後から活性酸素の量は、飛躍的に増大するのである。ベント芝の葉A,高麗芝の葉と、野芝の葉との混合物B,葉、茎、根を含む高麗芝と野芝との混合物Cをそれぞれ試料として加水分解並びに冷却処理を行って得られたそれぞれの抽出液にXODを0.1ml(リットル)添加し、それぞれの抽出液に生じる電流の変化を測定した。   The measurement results are shown below. FIG. 5 is a blank, and shows a temporal change in the amount of active oxygen produced in the active oxygen system when XOD is added. As is apparent from the figure, if there is no substance that prevents the generation of active oxygen by adding XOD, the amount of active oxygen increases dramatically after about 80 seconds have elapsed since the start of measurement. Bent turf leaf A, Goryo turf leaf and wild turf leaf mixture B, leaf stalk, root turf mixture C and wild turf mixture C obtained respectively by hydrolysis and cooling treatment 0.1 ml (liter) of XOD was added to each extract, and the change in current generated in each extract was measured.

その結果を順に図6〜8に示す。図6は、ベント芝の葉からの抽出液(実験A)、図7は、高麗芝の葉と、野芝の葉との混合物からの抽出液(実験B)、図8は、葉、茎、根を含む高麗芝と野芝との混合物からの抽出液(実験C)についての実験結果を示している。図中、Pは、試料中にXODを添加した時点を示している。測定開始後80秒経過した後に試料中にXODを添加した。それぞれの実験についての測定条件が違うために、各実験の測定結果の相互の関係を対比することはできないが、いずれの実験A〜Cにおいても、XODの添加時点で、過渡的に電流値が変化したが、その後XODの添加後、活性酸素の生成量は増加することがなく、むしろ低下してゆく傾向すら認められた。これによって、実験に用いた植物原料からの抽出液は抗酸化能を有していることが証明された。   The results are shown in FIGS. FIG. 6 shows an extract from bent turf leaves (Experiment A), FIG. 7 shows an extract from a mixture of Goose turf leaves and wild turf leaves (Experiment B), and FIG. 8 shows leaves and stems. The experimental result about the extract (experiment C) from the mixture of the ginseng and the grass which contains roots is shown. In the figure, P indicates the time when XOD was added to the sample. After 80 seconds from the start of measurement, XOD was added to the sample. Since the measurement conditions for each experiment are different, the mutual relationship between the measurement results of each experiment cannot be compared. However, in any of experiments A to C, the current value transiently changes at the time of addition of XOD. However, after the addition of XOD, the amount of active oxygen produced did not increase, but rather tended to decrease. This proved that the extract from the plant raw material used in the experiment has antioxidant ability.

本発明の方法によれば、植物の細胞壁に含まれる抗酸化成分を変質させることなく抽出することができ、抽出液に含まれる抗酸化成分は優れた抗酸化能を有し、本発明方法によって得られた抗酸化成分組成物を含む抽出液を薬品、食品として摂取することにより、病気の治療は勿論、シミ,そばかすの発生を抑え、美容,健康の維持,老化防止などに大いに期待できる。   According to the method of the present invention, the antioxidant component contained in the cell wall of the plant can be extracted without alteration, and the antioxidant component contained in the extract has an excellent antioxidant ability. By taking the extract containing the obtained antioxidant component composition as a medicine or food, it can be expected not only to treat diseases but also to suppress the occurrence of spots and freckles, and to maintain beauty, health and prevent aging.

本発明方法を実施する装置の概念図である。It is a conceptual diagram of the apparatus which implements the method of this invention. 本発明方法を実施する装置の構成図である。It is a block diagram of the apparatus which implements the method of this invention. 本発明方法のフローを示す図である。It is a figure which shows the flow of this invention method. セルロースの分解の様子を示す図である。It is a figure which shows the mode of decomposition | disassembly of a cellulose. XODの活性酸素系の活性酸素生成量の時間的変化を示す図である。It is a figure which shows the time change of the active oxygen production amount of the active oxygen system of XOD. ベント芝の葉からの抽出液にXODを添加したときの活性酸素の変化を示す図である。It is a figure which shows the change of active oxygen when XOD is added to the extract from the leaf of bent turf. 高麗芝の葉と、野芝の葉との混合物からの抽出液にXODを添加したときの活性酸素の変化を示す図である。It is a figure which shows the change of an active oxygen when XOD is added to the extract from the mixture of a leaf of a Korean turf and a leaf of a wild turf. 葉、茎、根を含む高麗芝と野芝との混合物からの抽出液にXODを添加したときの活性酸素の変化を示す図である。It is a figure which shows the change of an active oxygen when XOD is added to the extract from the mixture of the ginseng and the wild turf containing a leaf, a stem, and a root.

符号の説明Explanation of symbols

1 処理チャンバー
2 抽出管
3 冷却塔
4 循環ポンプ
5 加熱ヒータ
6 蒸気戻り口
7 蒸気送出口
8 投入口
9 排出口
10 攪拌羽根
DESCRIPTION OF SYMBOLS 1 Processing chamber 2 Extraction pipe 3 Cooling tower 4 Circulation pump 5 Heater 6 Steam return port 7 Steam delivery port 8 Input port 9 Outlet port 10 Stirring blade

Claims (1)

原料投入処理と、加水分解処理と、冷却処理とを有する植物に含まれた抗酸化成分の抽出方法であって、
原料投入処理は、植物原料を処理チャンバー内に投入し、処理チャンバーを密閉する処理であり、処理チャンバーは、植物原料を加熱する釜であり、処理チャンバーの送出側、戻り側が循環管路を形成する抽出管でつながれ、その管路内に冷却塔が接続され、冷却塔の上流側の管路内に循環ポンプが接続されたものであり、
加水分解処理は、処理チャンバー内の植物原料を130℃〜150℃の範囲で加熱し、植物原料自身が有する水分を蒸発させ、処理チャンバー内をその水蒸気の飽和水蒸気圧に保たせて5〜8時間植物原料を一定時間曝し、植物原料を加熱して加熱温度の飽和水蒸気圧のもとで植物組織を加水分解し、加水分解によって植物の細胞壁の高分子構造から開放された抗酸化成分を細胞内成分と共に水蒸気および処理チャンバー内に生成される植物原料の固形物中に取り込ませる処理であり、
冷却処理は、加水分解処理による植物原料の加熱終了後、送出側、戻り側の抽出管のバルブを開き、循環ポンプを起動して処理チャンバー内の水蒸気を抽出管内に吸引し、冷却塔を経由させて一部を凝結させ、余剰の水蒸気は再び処理チャンバー内に戻し、処理チャンバー内の水蒸気を冷却塔と処理チャンバー間で循環させ、冷却塔内に送り込まれた水蒸気を冷却して水蒸気中に含まれる抗酸化成分を細胞内成分と共に抽出し、一部は処理チャンバー内に生成される固形物に取り込んで収集する処理であることを特徴とする植物に含まれた抗酸化成分の抽出/収集方法。
A raw material charging process, the hydrolysis process, a method of extracting antioxidants contained in plants and a cooling process,
The raw material charging process is a process in which a plant raw material is put into a processing chamber and the processing chamber is sealed, and the processing chamber is a kettle for heating the plant raw material, and a circulation line is formed on the sending side and the return side of the processing chamber. Connected to the extraction pipe, a cooling tower is connected in the pipe, and a circulation pump is connected in the pipe upstream of the cooling tower,
In the hydrolysis treatment, the plant raw material in the processing chamber is heated in the range of 130 ° C. to 150 ° C. to evaporate the water contained in the plant raw material itself, and the processing chamber is maintained at the saturated water vapor pressure of the water vapor. The plant material is exposed for a certain period of time, the plant material is heated and the plant tissue is hydrolyzed under the saturated water vapor pressure of the heating temperature, and the antioxidant components released from the macromolecular structure of the plant cell wall by hydrolysis are converted into cells. It is a treatment to be taken into the solid material of the plant raw material generated in the treatment chamber with water vapor together with the internal components,
In the cooling process, after heating the plant raw material by hydrolysis, the valves on the extraction pipes on the delivery side and the return side are opened, the circulation pump is activated, and the water vapor in the processing chamber is sucked into the extraction pipe and passes through the cooling tower. The water vapor in the processing chamber is circulated between the cooling tower and the processing chamber, and the water vapor sent into the cooling tower is cooled to the water vapor. antioxidant components contained extracted with intracellular components, some extracts antioxidant components contained in the plant, which is a process of collecting incorporated into solid generated in the processing chamber / Collection method.
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