JP2010083810A - Method for producing extract - Google Patents

Method for producing extract Download PDF

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JP2010083810A
JP2010083810A JP2008255274A JP2008255274A JP2010083810A JP 2010083810 A JP2010083810 A JP 2010083810A JP 2008255274 A JP2008255274 A JP 2008255274A JP 2008255274 A JP2008255274 A JP 2008255274A JP 2010083810 A JP2010083810 A JP 2010083810A
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extract
extraction
solvent
volume
container
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Takeo Matsumura
健雄 松村
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Nitto Denko Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for producing an extract having little raffinate and high concentration of a solid solute easily, efficiently and at a low cost. <P>SOLUTION: The method for producing an extract includes filling a dry feed to be extracted in one or more solvent-permeable containers and extracting the solid solute by immersing the container in a solvent, wherein the volume of the container is smaller than that of the filled feed swollen by the solvent. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、被抽出物(例えば植物組織)からエキス成分を抽出するエキス抽出液の製造方法に関し、特に残渣の混入が少なく、固形分濃度の高いエキス抽出液を効率よく低コストで得られる方法に関する。   The present invention relates to a method for producing an extract extract that extracts an extract component from an extract (for example, plant tissue), and in particular, a method for efficiently obtaining an extract extract having a high solid content with low residue contamination and low cost. About.

従来、植物組織からエキス成分を抽出する場合は、植物組織を、抽出タンクにそのまま投入し、水やアルコールなどの溶媒を用いて、必要により、攪拌、加温しながらエキス成分を抽出している(特許文献1)。ここで使用される植物組織原料は、一般に保存性、つまり腐敗などの問題を考慮して、予め乾燥させたものが使用されている。また、乾燥させた植物組織は細胞が破壊されているので有用成分の抽出効率を向上させることができる。   Conventionally, when extracting an extract component from plant tissue, the plant tissue is put into an extraction tank as it is, and the extract component is extracted while stirring and heating as necessary using a solvent such as water or alcohol. (Patent Document 1). The plant tissue raw material used here is generally dried in advance in consideration of problems such as storage stability, that is, spoilage. Moreover, since the dried plant tissue has cells destroyed, the extraction efficiency of useful components can be improved.

しかし、乾燥した植物組織は、乾燥前の植物の含水率が高いために非常に吸液性が高く、抽出に用いる溶媒を多量に吸収して膨潤する。このため、比較的少量の抽出溶媒を用いた抽出では、エキス抽出液の回収量が減り、エキス抽出液から溶媒を除去した後の残渣であるエキス固形分抽出量が少なく、エキス成分の抽出率が悪くなるといった問題がある。   However, the dried plant tissue is very liquid-absorbing due to the high moisture content of the plant before drying, and swells by absorbing a large amount of the solvent used for extraction. For this reason, in extraction using a relatively small amount of extraction solvent, the amount of extract extract recovered is reduced, the amount of extract solids that is the residue after removal of the solvent from the extract extract is small, and the extraction rate of extract components There is a problem that becomes worse.

高いエキス成分の抽出量を得るためには、乾燥した植物組織の重量に対して20倍量程度の多量の抽出溶媒が必要になる。しかしその場合には、多量の抽出溶媒のためにエキス抽出液中のエキス固形分濃度が低下し、エキス成分を濃縮する際に、濃縮のためのエネルギーコストが高くなる他、濃縮効率が悪くなるといった問題が生じる。   In order to obtain a high extraction amount of the extract component, a large amount of extraction solvent of about 20 times the weight of the dried plant tissue is required. However, in that case, the extract solid content concentration in the extract extract decreases due to a large amount of the extraction solvent, and when concentrating the extract components, the energy cost for concentration increases and the concentration efficiency deteriorates. Problems arise.

また、抽出工程の後、植物組織や残渣の分離が必要であり、コストが高くなる。一般には、抽出タンク内へろ過板等が設置されるが、装置が複雑になる他、抽出タンクの洗浄に手間が掛かり、コストが高くなるといった問題がある。   Moreover, after an extraction process, isolation | separation of a plant tissue and a residue is required, and cost becomes high. In general, a filter plate or the like is installed in the extraction tank, but there are problems that the apparatus becomes complicated and that the extraction tank needs to be cleaned and the cost is increased.

特許第3841458号公報Japanese Patent No. 3841458

上記事情に鑑み、本発明は、残渣の混入が少なく、エキス固形分濃度の高いエキス抽出液を、容易に効率よく低コストで得られるエキス抽出液の製造方法を提供することを目的とする。   In view of the above circumstances, an object of the present invention is to provide a method for producing an extract extract that can easily and efficiently obtain an extract extract having a high concentration of extract solids with little residue mixing.

本発明者は、上記目的を達成すべく鋭意研究を重ねた結果、乾燥した被抽出物を、該被抽出物の膨潤体積よりも小さい容器に封入して抽出すると、少量の抽出溶媒を用いた場合でも高いエキス抽出率が得られ、エキス固形分濃度の高いエキス抽出液を製造することに成功した。また、被抽出物を複数の容器に小分けして抽出した場合に特に高いエキス抽出率が得られることを見出した。
本発明者はこれらの知見に基づいてさらに検討を重ねた結果、本発明を完成するに至った。
As a result of intensive studies to achieve the above object, the present inventor used a small amount of extraction solvent when the dried extract was sealed in a container smaller than the swelling volume of the extract and extracted. Even in the case, a high extract extraction rate was obtained, and an extract extract having a high extract solid content concentration was successfully produced. In addition, it has been found that a particularly high extract extraction rate can be obtained when the extraction object is divided into a plurality of containers and extracted.
As a result of further studies based on these findings, the present inventor has completed the present invention.

すなわち、本発明は以下のとおりである。
(1)乾燥した被抽出物を1以上の溶媒透過性の容器内に封入し、該容器を溶媒に浸漬させてエキス固形分を溶媒抽出することを含むエキス抽出液の製造方法であって、該容器の容積が、封入される被抽出物の溶媒による膨潤体積よりも小さいことを特徴とする方法。
(2)容器の容積が、封入される被抽出物の膨潤体積の0.6〜0.9倍である、(1)記載の方法。
(3)被抽出物が植物組織である、(1)または(2)記載の方法。
(4)植物組織が薬用人参カルスである、(3)記載の方法。
(5)上記(1)〜(4)のいずれかに記載の方法により得られるエキス抽出液を濃縮することを特徴とする、エキス固形分濃縮物の製造方法。
That is, the present invention is as follows.
(1) A method for producing an extract extract comprising enclosing a dried extract in one or more solvent-permeable containers, immersing the container in a solvent, and extracting the extract solids with a solvent, A method characterized in that the volume of the container is smaller than a swelling volume of the encapsulated extract by a solvent.
(2) The method according to (1), wherein the volume of the container is 0.6 to 0.9 times the swelling volume of the extract to be encapsulated.
(3) The method according to (1) or (2), wherein the extract is a plant tissue.
(4) The method according to (3), wherein the plant tissue is ginseng callus.
(5) A method for producing an extract solids concentrate, comprising concentrating an extract extract obtained by the method according to any one of (1) to (4) above.

本発明によれば、比較的少量の抽出溶媒を用いて、エキス固形分濃度の高いエキス抽出液を得ることができるので、エキス抽出液の濃縮に要するコストや労力を軽減することができ、容易に効率良く低コストで得られるエキス抽出液の製造方法を提供することができる。また、残渣の混入の少ないエキス抽出液が得られるため、抽出後の工程を簡略化することができる。   According to the present invention, an extract extract with a high extract solid content concentration can be obtained using a relatively small amount of an extraction solvent, so that the cost and labor required for concentration of the extract extract can be reduced, and it is easy. In addition, it is possible to provide a method for producing an extract extract that can be obtained efficiently and at low cost. Moreover, since the extract extract with little residue mixing is obtained, the post-extraction process can be simplified.

本発明は、乾燥した被抽出物を1以上の溶媒透過性の容器内に封入し、該容器を溶媒に浸漬させてエキス固形分を溶媒抽出することを含むエキス抽出液の製造方法であって、該容器の容積が、封入される被抽出物の溶媒による膨潤体積よりも小さいことを特徴とする方法を提供するものである。   The present invention is a method for producing an extract extract comprising enclosing a dried extract in one or more solvent-permeable containers and immersing the container in a solvent to extract the extract solids by solvent. The method is characterized in that the volume of the container is smaller than the swelling volume of the encapsulated extract by the solvent.

本発明における被抽出物としては、溶媒に膨潤する限り特に限定されないが、植物組織又は動物系材料が挙げられる。高い膨潤性の観点より、植物組織が好ましく、植物組織としては、例えば、生薬類(蒼朮、厚朴、陳皮、甘草、生姜、大棗、香附子、縮砂、芍薬、当帰、川キュウ、地黄、茯苓、桂皮、杜仲、人参、延胡索、茴香、良姜、阿片等)、コーヒー類、茶類、果実類、穀物類もしくは焙煎穀物類(麦等)、香辛料類、ビーンズ類、ナッツ類、ハーブ類、海草類等を挙げることができる。
中でも、乾燥させた生薬が好ましく、より好ましくは薬用人参(高麗人参、田七人参、チクセツ人参、アメリカ人参、三七人参、シベリア人参等)の乾燥物、特に好ましくは高麗人参の乾燥物である。また、植物組織は、ファーメンター等の培養装置により組織培養されたカルスを好ましく用いることができる。
最も好ましい被抽出物は、組織培養された高麗人参カルスの乾燥物である。
The extract in the present invention is not particularly limited as long as it swells in a solvent, and examples thereof include plant tissues or animal materials. From the viewpoint of high swellability, a plant tissue is preferable, and examples of plant tissues include herbal medicines (acupuncture, magnolia, crust, licorice, ginger, oats, garlic, shredded sand, glaze, Toki, Kawakyu, Ground yellow, cocoon, cinnamon bark, cinnamon, carrots, ryoko, musk, bonito, opium, etc.), coffee, teas, fruits, cereals or roasted cereals (wheat etc.), spices, beans, nuts , Herbs and seaweeds.
Among them, dried herbal medicine is preferable, more preferably dried ginseng (ginseng, ginseng, chixetsu ginseng, American ginseng, ginseng, Siberian ginseng, etc.), particularly preferably dried ginseng. . As the plant tissue, callus cultured in a culture apparatus such as a fermenter can be preferably used.
The most preferable extract is a dried ginseng callus tissue-cultured.

本発明における乾燥した被抽出物は、天日、加熱乾燥、熱風乾燥、真空乾燥、凍結乾燥、送風乾燥等により乾燥させたものであり、天日または熱風乾燥させたものが好ましい。例えば薬用人参は、薬用人参そのものまたは組織培養により得られたカルスを天日または熱風乾燥、好ましくは30〜90℃、より好ましくは50〜85℃の温度下で緩徐に乾燥させる。乾燥温度が90℃を超える高温下で乾燥を行うと、薬用人参特有の香りが失われたり、含有される有効成分が分解するおそれもあり、乾燥温度が30℃未満の低温下で乾燥を行うと、長時間を要するので乾燥中に腐敗してしまうおそれがある。
本発明における乾燥した被抽出物とは、含水率が1〜15重量%であり、2〜10重量%が好ましい。
例えば乾燥後の薬用人参(カルスを含む)の含水率は、乾燥コストや保存性の観点から2〜9重量%、特に3〜6重量%が好ましい。
The dried extract in the present invention is dried by sunlight, heat drying, hot air drying, vacuum drying, freeze drying, blow drying, or the like, and is preferably sun or hot air dried. For example, the ginseng itself slowly drys the ginseng itself or the callus obtained by tissue culture at a temperature of 30 to 90 ° C., more preferably 50 to 85 ° C., by sun or hot air drying. If drying is performed at a high temperature exceeding 90 ° C, the scent peculiar to ginseng may be lost or the contained active ingredient may be decomposed. Therefore, drying is performed at a low temperature of less than 30 ° C. And it takes a long time, so there is a risk of decay during drying.
The dried extract in the present invention has a water content of 1 to 15% by weight, preferably 2 to 10% by weight.
For example, the moisture content of ginseng (including callus) after drying is preferably 2 to 9% by weight, particularly 3 to 6% by weight from the viewpoint of drying cost and storage stability.

また、被抽出物は、そのまま用いることができるが、被抽出物の溶媒による膨潤性を損なわない範囲で、適当な大きさに細分化処理(切断、粉砕等)したものを用いることもできる。これにより、エキス成分の抽出率を向上させることができる。例えば、被抽出物として薬用人参カルスを用いる場合、そのままあるいは粉砕器や石臼などで粉砕した後、ふるい等で分画して得られる平均粒径500〜20000μm、好ましくは1000〜10000μmのカルスを好ましく用いることができる。
また、披抽出物の大きさによって抽出されるエキス成分が異なる場合は、目的のエキス成分に応じて被抽出物の大きさを選択すればよい。
Further, the extract can be used as it is, but it is also possible to use a product that has been subdivided (cut, pulverized, etc.) into an appropriate size as long as the swellability of the extract by the solvent is not impaired. Thereby, the extraction rate of an extract component can be improved. For example, when using ginseng callus as an extract, callus having an average particle diameter of 500 to 20000 μm, preferably 1000 to 10,000 μm, obtained as it is or after being pulverized with a pulverizer or a stone mortar, is preferably used. Can be used.
Moreover, what is necessary is just to select the magnitude | size of to-be-extracted object according to the target extract component, when the extract component extracted according to the magnitude | size of an extract is different.

本発明における溶媒透過性の容器とは、溶媒透過性を有しかつ被抽出物を封入し得るものであり、形状は特に限定されない。被抽出物を容器内に封入することによって、残渣の混入を防ぐとともに、被抽出物の溶媒で膨潤する力を抑圧するので、容易に効率よくエキス成分を抽出することができる。溶媒透過性の容器としては、溶媒透過性の袋、ケージ、筒等が挙げられ、溶媒透過性の袋が好ましく使用できる。
また、本発明では、1以上の溶媒透過性の容器を使用する。容器の数を増やし、被抽出物を複数の容器に小分けして抽出すると、エキス成分の抽出率が高くなり、効率的な抽出が可能となり好ましい。
The solvent-permeable container in the present invention has solvent permeability and can enclose an extract, and its shape is not particularly limited. By encapsulating the extract in the container, it is possible to extract the extract component easily and efficiently because the mixture of residues is prevented and the swelling force of the extract with the solvent is suppressed. Examples of the solvent permeable container include a solvent permeable bag, a cage, and a cylinder, and a solvent permeable bag can be preferably used.
In the present invention, one or more solvent-permeable containers are used. It is preferable to increase the number of containers and divide the extraction object into a plurality of containers for extraction, thereby increasing the extraction rate of the extract component and enabling efficient extraction.

また、溶媒透過性の容器の素材としては、溶媒を透過する機能を発揮し得る限り特に限定されないが、布、メッシュクロスは、良好な溶媒透過性が得られるため好ましい。ここで、メッシュクロスとしては、ナイロンメッシュクロス、ポリエステルメッシュクロス、ポリエチレンメッシュクロス、ポリプロピレンメッシュクロス、テフロン(登録商標)メッシュクロス、金属製メッシュクロス(例えばステンレスメッシュクロス)を好ましく挙げることができる。
この中でも特に、単層のナイロンメッシュクロスは、溶媒の透過性、耐薬品性に優れ、好ましい。
The material of the solvent-permeable container is not particularly limited as long as it can exhibit the function of permeating the solvent, but cloth and mesh cloth are preferable because good solvent permeability can be obtained. Here, preferred examples of the mesh cloth include nylon mesh cloth, polyester mesh cloth, polyethylene mesh cloth, polypropylene mesh cloth, Teflon (registered trademark) mesh cloth, and metal mesh cloth (for example, stainless steel mesh cloth).
Among these, a single-layer nylon mesh cloth is particularly preferable because of excellent solvent permeability and chemical resistance.

また、溶媒透過性の容器の目開きは、特に限定されないが、効率的に抽出する観点から、被抽出物の残渣が目開きから漏れない程度に粗いものが好ましく、通常5〜5000μmであり、好ましくは10〜1000μmである。   Further, the opening of the solvent-permeable container is not particularly limited, but from the viewpoint of efficient extraction, a coarse one is preferable to the extent that the residue of the extraction object does not leak from the opening, and is usually 5 to 5000 μm, Preferably it is 10-1000 micrometers.

また、溶媒透過性の容器へ、被抽出物を、被抽出物が溶媒を吸収し、膨潤したときに容器がはち切れない程度の量を封入することが好ましい。従って、溶媒透過性の容器の容積は、被抽出物の溶媒で膨潤する力を抑圧し、効率よくエキス成分を抽出する観点から、通常封入される被抽出物の膨潤体積よりも小さく、通常封入される被抽出物の膨潤体積の0.35〜0.98倍であり、0.6〜0.9倍であることが好ましい。   Further, it is preferable to enclose the extract in a solvent permeable container in such an amount that the extract does not tear off when the extract absorbs the solvent and swells. Therefore, the volume of the solvent-permeable container is smaller than the swelling volume of the extract to be normally enclosed from the viewpoint of efficiently extracting the extract component from suppressing the force of the extract to swell with the solvent. The swelling volume of the extract to be extracted is 0.35 to 0.98 times, and preferably 0.6 to 0.9 times.

具体的に、容器の容積は以下のように決定することができる。
例えば、被抽出物(乾燥植物組織10g)の膨潤体積が100mLの場合には、60〜90mLの容器、乾燥植物組織100kgからエキス成分を抽出する場合には、膨潤体積が1000Lになることから、その0.6〜0.9倍の容積、つまり600〜900Lの容積の容器を用いればよい。
Specifically, the volume of the container can be determined as follows.
For example, when the extract volume (dry plant tissue 10 g) has a swelling volume of 100 mL, when the extract component is extracted from a 60-90 mL container, dry plant tissue 100 kg, the swelling volume becomes 1000 L. A container having a volume of 0.6 to 0.9 times, that is, a volume of 600 to 900 L may be used.

また、被抽出物の膨潤体積は、以下の方法を用いて測定することができる。
例えば、200mLのメスシリンダー内の被抽出物(乾燥植物組織10g)に対し、十分な量の抽出溶媒を加えて攪拌し、十分に膨潤させた後、メスシリンダーを静置して沈降した植物組織のメスシリンダーの目盛を読み取り、植物組織が抽出溶媒中で占める見掛け容積を測定する。
本発明においては、効率よくエキス成分を抽出する観点から、被抽出物が膨潤によって膨潤前の体積の1.2〜4倍、好ましくは 1.4〜3倍となることが好ましい。具体的には、薬用人参の場合、膨潤によって膨潤前の体積の1.6〜2.5倍であることが好ましい。
Moreover, the swelling volume of the to-be-extracted object can be measured using the following method.
For example, a sufficient amount of extraction solvent is added to an extract (200 g of dry plant tissue) in a 200 mL graduated cylinder, and the mixture is stirred sufficiently to swell, then the graduated cylinder is allowed to settle and settle. Measure the apparent volume of plant tissue in the extraction solvent.
In the present invention, from the viewpoint of efficiently extracting the extract component, it is preferable that the extractables become 1.2 to 4 times, preferably 1.4 to 3 times the volume before swelling due to swelling. Specifically, in the case of ginseng, it is preferably 1.6 to 2.5 times the volume before swelling due to swelling.

また、本発明における溶媒としては、被抽出物によっても異なるが、水、メタノール、エタノール、プロピレングリコール、1,3−ブチレングリコール、アセトンまたはそれらの混合物が挙げられ、水またはエタノールを好ましく用いることができる。具体的には、薬用人参の場合、水または水/エタノール1:1の混合物が好ましい。   Moreover, as a solvent in this invention, although it changes also with to-be-extracted, water, methanol, ethanol, propylene glycol, 1, 3- butylene glycol, acetone, or those mixtures are mentioned, It is preferable to use water or ethanol. it can. Specifically, for ginseng, water or a water / ethanol 1: 1 mixture is preferred.

また、抽出条件は、被抽出物の種類若しくは量に応じて適宜決定することができる。抽出は、加温する方が抽出効率はよく、抽出温度は、30〜95℃、好ましくは60〜85℃で実施することができる。抽出時間は、温度によって異なるが、15〜360分、好ましくは30〜90分で実施することができる。被抽出物に対する抽出溶媒の比は、被抽出物の重量に対して5〜30倍量、好ましくは8〜15倍量の抽出溶媒にて実施することができる。
好ましい抽出条件の一例は、被抽出物として乾燥植物組織の重量に対し、抽出溶媒として10倍量の水を加え、80℃まで加温して1時間の抽出操作を行うことが好ましい。
Further, the extraction conditions can be appropriately determined according to the type or amount of the extraction object. The extraction can be carried out at a temperature of 30 to 95 ° C., preferably 60 to 85 ° C., when the extraction is heated. Although extraction time changes with temperature, it can implement in 15 to 360 minutes, Preferably it is 30 to 90 minutes. The ratio of the extraction solvent to the extract can be 5 to 30 times, preferably 8 to 15 times the amount of the extraction solvent with respect to the weight of the extract.
As an example of preferable extraction conditions, it is preferable to add 10 times the amount of water as an extraction solvent with respect to the weight of the dried plant tissue as an extract, and heat the mixture to 80 ° C. for 1 hour.

また、抽出操作は、任意の回数で実施することができ、抽出操作を複数回実施する場合には、同一の抽出条件(抽出温度、抽出時間等)で抽出操作を複数回実施することもでき、抽出条件を変更して実施することもできる。
また、被抽出物を封入した容器を抽出溶媒中に静置させた状態で抽出してもよいが、該容器を用いて抽出溶媒を攪拌してもよい。ただし、容器が破れない程度で攪拌する必要がある。または、抽出溶媒をポンプで循環させてもよい。
抽出操作後は、残渣の混入が少ないため、特にろ過工程を必要とせずに、エキス抽出液を得ることができる。
In addition, the extraction operation can be performed any number of times, and when the extraction operation is performed a plurality of times, the extraction operation can be performed a plurality of times under the same extraction conditions (extraction temperature, extraction time, etc.). The extraction conditions can also be changed.
The extraction may be performed in a state where the container in which the extraction object is sealed is allowed to stand in the extraction solvent, but the extraction solvent may be stirred using the container. However, it is necessary to stir so that the container does not break. Alternatively, the extraction solvent may be circulated with a pump.
Since there is little residue mixing after the extraction operation, an extract extract can be obtained without particularly requiring a filtration step.

本発明の方法により得られるエキス抽出液は、溶媒透過性の容器の容積を、封入される被抽出物の膨潤体積よりも小さくしたため、被抽出物の溶媒で膨潤する力が抑圧され、抽出溶媒添加量に対するエキス抽出液回収量は高い。このため、エキス固形分濃度を向上させたい場合は、抽出溶媒添加量を少なくすることが可能となり、少量の抽出溶媒で効率的な抽出を行うことが可能である。その結果、濃縮のためのエネルギーコストを低く抑えることができる。
また、得られたエキス抽出液を適当なろ材を用いて予めろ過してから濃縮してもよいが、残渣の混入が少ないので、そのまま濃縮することもでき、抽出後の工程を簡略化することができる。これによって低コストでエキスを提供することができる。
In the extract obtained by the method of the present invention, the volume of the solvent-permeable container is made smaller than the swelling volume of the extract to be enclosed, so that the force of swelling with the solvent of the extract is suppressed, and the extract solvent The amount of extract extract recovered relative to the amount added is high. For this reason, when it is desired to improve the extract solid content concentration, it is possible to reduce the amount of extraction solvent added, and it is possible to perform efficient extraction with a small amount of extraction solvent. As a result, the energy cost for concentration can be kept low.
In addition, the obtained extract extract may be concentrated after pre-filtering using a suitable filter medium, but it can be concentrated as it is because there is little contamination of the residue, and the process after extraction is simplified. Can do. Thereby, an extract can be provided at low cost.

本発明の別の態様として、上述したエキス抽出液を濃縮することを特徴とするエキス固形分濃縮物の製造方法を提供する。
本発明における抽出物を濃縮する方法としては、加熱濃縮、減圧濃縮、噴霧濃縮、真空濃縮、冷凍濃縮等が挙げられ、真空濃縮、噴霧濃縮が好ましい。
最も好ましい濃縮方法は真空濃縮であり、例えば、遠心式薄膜真空蒸発装置に抽出液を連続供給し、真空下で蒸発温度70〜85℃にて濃縮を行うことが好ましい。
また、本発明におけるエキス固形分濃縮物とは、本発明により得られるエキス抽出液を上述の濃縮方法によって濃縮し、固形分濃度40〜80%となるように調製したものである。
本発明の方法により製造されるエキス固形分濃縮物は、そのままで、または適当な担体、添加物とともに製剤化処理、加工処理、殺菌処理等を行うことによって、医薬製剤、化粧品、食品等とすることができる。
As another aspect of the present invention, there is provided a method for producing an extract solids concentrate characterized in that the extract extract described above is concentrated.
Examples of the method for concentrating the extract in the present invention include heat concentration, reduced pressure concentration, spray concentration, vacuum concentration, and freeze concentration, and vacuum concentration and spray concentration are preferred.
The most preferable concentration method is vacuum concentration. For example, it is preferable to continuously supply the extract to a centrifugal thin film vacuum evaporator and perform concentration at an evaporation temperature of 70 to 85 ° C. under vacuum.
The extract solid concentrate in the present invention is prepared by concentrating the extract extract obtained by the present invention by the above-described concentration method so that the solid concentration is 40 to 80%.
The extract solids concentrate produced by the method of the present invention is used as a pharmaceutical preparation, cosmetics, food, etc. as it is or by carrying out formulation treatment, processing treatment, sterilization treatment, etc. together with appropriate carriers and additives. be able to.

以下、本発明について、実施例を挙げてさらに具体的に説明する。本発明はこれらにより何ら限定されるものではない。   Hereinafter, the present invention will be described more specifically with reference to examples. The present invention is not limited by these.

実施例1
被抽出物として高麗人参カルスの乾燥品(乾燥品10gの膨潤体積が90mL、含水率3.5%、平均粒径3000μm)7.5gを、目開き180μmのナイロンメッシュ製の袋に充填して封をした。ここで、袋の容積は、48mL(7.5gの高麗人参カルスの乾燥品の膨潤体積の0.71倍)である。
この充填物を300mLのガラス製ビーカーに入れ、ここに抽出溶媒として精製水80gを加え、80℃の恒温水槽にビーカーを浸して60分間抽出操作を行った。
抽出後、エキス抽出液を室温まで冷却し、冷却したエキス抽出液の重量を測定した(エキス抽出液回収量)。
さらに、ろ紙でろ過したエキス抽出液10gを秤量瓶にとり、105℃の恒温器内で水分を蒸発乾固させ、乾固物の重量を測定することにより、エキス抽出液中のエキス固形分濃度および高麗人参カルスの乾燥品7.5gから得られるエキス固形分抽出量を求めた。また、高麗人参カルスの乾燥品7.5gに対するエキス固形分抽出量からエキス固形分抽出率を求めた。
Example 1
As an extract, 7.5 g of dried ginseng callus (swelled volume of 10 g of dried product is 90 mL, moisture content of 3.5%, average particle size of 3000 μm) is filled in a bag made of nylon mesh with an opening of 180 μm. Sealed. Here, the volume of the bag is 48 mL (0.71 times the swelling volume of the dried product of 7.5 g of ginseng callus).
This filling material was put into a 300 mL glass beaker, 80 g of purified water was added thereto as an extraction solvent, and the beaker was immersed in a constant temperature water bath at 80 ° C. for extraction for 60 minutes.
After extraction, the extract extract was cooled to room temperature, and the weight of the cooled extract extract was measured (extract extract recovery amount).
Furthermore, 10 g of the extract extract filtered through a filter paper is taken into a weighing bottle, the water is evaporated to dryness in a thermostatic chamber at 105 ° C., and the weight of the dried product is measured, whereby the extract solid concentration in the extract extract and The amount of extract solid extract obtained from 7.5 g of dried ginseng callus was determined. Moreover, extract solid content extraction rate was calculated | required from the amount of extract solid extract with respect to 7.5 g of dried ginseng callus.

実施例2
実施例1で用いた高麗人参カルスの乾燥品7.5gを、目開き180μmのナイロンメッシュ製の袋に3.75gずつ2袋に充填して封をした。袋の容積は、24mL(3.75gの高麗人参カルスの乾燥品の膨潤体積の0.71倍)である。それ以外は実施例1と同様にして行った。
Example 2
7.5 g of dried ginseng callus used in Example 1 was filled in a nylon mesh bag with an opening of 180 μm in two bags and sealed. The volume of the bag is 24 mL (0.71 times the swelling volume of the dried product of 3.75 g of ginseng callus). Other than that was carried out in the same manner as in Example 1.

実施例3
実施例1で用いた高麗人参カルスの乾燥品7.5gを、目開き180μmのナイロンメッシュ製の袋に2.5gずつ3袋に充填して封をした。袋の容積は、16mL(2.5gの高麗人参カルスの乾燥品の膨潤体積の0.71倍)である。それ以外は、実施例1と同様にして行った。
Example 3
7.5 g of the dried ginseng callus used in Example 1 was filled into 2.5 bags of nylon mesh bags having an opening of 180 μm, and sealed in three bags. The volume of the bag is 16 mL (0.71 times the swelling volume of the dried product of 2.5 g of ginseng callus). Otherwise, the same procedure as in Example 1 was performed.

実施例4
高麗人参カルスの乾燥品(乾燥品10gの膨潤体積が95mL、含水率4%、平均粒径3000μm)75kgを、目開き180μmのナイロンメッシュ製の袋に、4.2kgずつ18袋に充填し封をした。1袋の容積は、35Lであり、高麗人参カルスの乾燥品の膨潤体積の0.88倍である〔35000÷(4200÷10×95)=0.88〕。
これを1200Lのステンレス製の抽出タンクに入れ、ここに精製水800kgを加え、80℃に加温して60分間抽出操作を行った。このとき、抽出溶媒を循環ポンプによりタンク下部からタンク上部まで循環させた。
抽出後、エキス抽出液を室温まで冷却し、冷却したエキス抽出液の重量を測定した。
さらに、ろ紙によりろ過したエキス抽出液10gを秤量瓶にとり、105℃の恒温器中で水分を蒸発乾固させ、乾固物の重量を測定することにより、エキス抽出液中のエキス固形分濃度および高麗人参カルスの乾燥品75kgから得られるエキス固形分抽出量を求めた。また、高麗人参カルスの乾燥品75kgに対するエキス固形分抽出量からエキス固形分抽出率を求めた。
Example 4
75 kg of dried ginseng callus (swelled volume of 10 g of dried product is 95 mL, moisture content 4%, average particle size 3000 μm) is packed into 18 bags of 4.2 kg each in a bag made of nylon mesh with an opening of 180 μm and sealed. Did. The volume of one bag is 35 L, which is 0.88 times the swelling volume of the dried ginseng callus [35000 ÷ (4200 ÷ 10 × 95) = 0.88].
This was put into a 1200 L stainless steel extraction tank, 800 kg of purified water was added thereto, and the mixture was heated to 80 ° C. and extracted for 60 minutes. At this time, the extraction solvent was circulated from the lower tank to the upper tank by a circulation pump.
After extraction, the extract extract was cooled to room temperature, and the weight of the cooled extract extract was measured.
Furthermore, 10 g of the extract extract filtered through a filter paper is placed in a weighing bottle, the water is evaporated to dryness in a thermostat at 105 ° C., and the weight of the dried product is measured to determine the concentration of extract solids in the extract extract and The amount of extract solid extract obtained from 75 kg of dried ginseng callus was determined. Moreover, extract solid content extraction rate was calculated | required from the extract solid content extraction amount with respect to 75 kg of dried products of ginseng callus.

比較例1〜3
実施例1で用いた高麗人参カルスの乾燥品7.5gを袋に入れず、そのまま300mLのビーカーに入れ、ここに精製水を比較例1では80g、比較例2では120g、比較例3では160g加える以外は実施例1と同様にして行った。
なお、エキス抽出液は、ステンレス製メッシュでカルスを濾して回収した。
Comparative Examples 1-3
7.5 g of dried ginseng callus used in Example 1 is not put in a bag, but is put in a 300 mL beaker as it is, and purified water is 80 g in Comparative Example 1, 120 g in Comparative Example 2, 160 g in Comparative Example 3 The procedure was the same as in Example 1 except for the addition.
The extract extract was recovered by filtering the callus with a stainless steel mesh.

表1に、実施例1〜4および比較例1〜3の結果を示す。
実施例1〜4では、エキス抽出液は褐色の透明な液体として得られた。また、実施例1〜4では、抽出溶媒添加量に対するエキス抽出液回収量は高かった。このため、さらに効率的な抽出を行いたい場合は、抽出溶媒添加量を少なくすることが可能であり、これによって、エキス固形分濃度を向上させ濃縮効率を高めることができ、少量の抽出溶媒で効率的な抽出を行うことが可能である。
また、実施例1〜3では、同じ抽出溶媒添加量が80gである比較例1よりもエキス固形分抽出量が高く、袋の数を増すほどエキス固形分抽出量が高かった。このため比較例2、3のように、抽出溶媒添加量を増やさずに、高いエキス固形分抽出量が得られ、効率的な抽出を行うことができた。また、実施例4は、実生産機スケールで実施したものであるが、実施例4においても、実施例1〜3と同様に高いエキス固形分抽出量が得られた。
Table 1 shows the results of Examples 1 to 4 and Comparative Examples 1 to 3.
In Examples 1 to 4, the extract extract was obtained as a brown transparent liquid. Moreover, in Examples 1-4, the extract extract recovery amount with respect to the extraction solvent addition amount was high. For this reason, if more efficient extraction is desired, the amount of extraction solvent added can be reduced, which can improve the concentration of extract solids and increase the concentration efficiency, with a small amount of extraction solvent. It is possible to perform efficient extraction.
Moreover, in Examples 1-3, the extract solid content extraction amount was higher than the comparative example 1 whose same extraction solvent addition amount is 80 g, and the extract solid content extraction amount was so high that the number of bags was increased. Therefore, as in Comparative Examples 2 and 3, a high extract solid content extraction amount was obtained without increasing the extraction solvent addition amount, and efficient extraction could be performed. Moreover, although Example 4 was implemented on the actual production machine scale, also in Example 4, high extract solid content extraction amount was obtained similarly to Examples 1-3.

これに対し、比較例1〜3では、エキス抽出液は褐色のやや濁りのある液体であり、夾雑物(細胞のカス)が含まれていた。
また、比較例1では、大半の水(抽出溶媒)が被抽出物である乾燥植物組織に吸収され、回収できたエキス抽出液量は少なくなった他、エキス固形分抽出量も少なくなった。
比較例2、3では、抽出溶媒添加量を増やすことによって、比較例1よりもエキス固形分抽出量は増加したが、エキス抽出液中のエキス固形分濃度が低くなった。
比較例1〜3では、乾燥植物組織による抽出溶媒の吸収が高く、抽出溶媒添加量に対するエキス抽出液回収量は低いため、実施例1〜4のように抽出溶媒添加量を少なくし、エキス固形分濃度を向上させることはできない。従って、抽出には多量の抽出溶媒を要することにより、回収されたエキス抽出液の濃縮に多大な手間を要するとともにエネルギーコストが高くなるほか、濃縮するための装置の運転コストが高くなるため、好ましくなかった。
On the other hand, in Comparative Examples 1 to 3, the extract extract was a brownish and slightly turbid liquid, and contained impurities (cell residue).
Further, in Comparative Example 1, most of the water (extraction solvent) was absorbed by the dry plant tissue as the extract, and the amount of extract extract that could be recovered was reduced, and the amount of extract solid extract was also reduced.
In Comparative Examples 2 and 3, the amount of extract solid extract increased from that of Comparative Example 1 by increasing the amount of extraction solvent added, but the extract solid concentration in the extract extract was lowered.
In Comparative Examples 1 to 3, since the absorption of the extraction solvent by the dried plant tissue is high and the extract extract recovery amount relative to the addition amount of the extraction solvent is low, the extraction solvent addition amount is reduced as in Examples 1 to 4, and the extract solid The partial concentration cannot be improved. Therefore, the extraction requires a large amount of extraction solvent, which requires a lot of time and effort for concentrating the recovered extract extract and increases the energy cost. There wasn't.

また、実施例1〜4では、抽出後の植物組織は抽出容器から袋ごと取り出せばよく、容器の洗浄が容易であるのに対して、比較例では抽出容器の壁面に付着した植物組織を、水等を用いて洗い流す操作や、洗い流された植物組織を廃棄のために濾す操作が必要となり、容器の洗浄に手間が掛かり好ましくなかった。   Moreover, in Examples 1-4, the plant tissue after extraction should just take out the bag from an extraction container, and it is easy to wash | clean a container, In contrast, in the comparative example, the plant tissue adhering to the wall surface of the extraction container, An operation of washing with water or the like and an operation of filtering the washed plant tissue for disposal are required, which is not preferable because it takes time and effort to wash the container.

Figure 2010083810
Figure 2010083810

本発明によれば、残渣の混入が少なく、エキス固形分濃度の高いエキス抽出液を、容易に効率よく低コストで得られるエキス抽出液が製造でき、高麗人参等のエキス抽出液を効率的に製造できる。   According to the present invention, it is possible to produce an extract extract that can be obtained easily and efficiently at a low cost, with an extract extract having a low concentration of residue and a high concentration of extract solids, and efficiently extracting an extract extract such as ginseng. Can be manufactured.

Claims (5)

乾燥した被抽出物を1以上の溶媒透過性の容器内に封入し、該容器を溶媒に浸漬させてエキス固形分を溶媒抽出することを含むエキス抽出液の製造方法であって、該容器の容積が、封入される被抽出物の溶媒による膨潤体積よりも小さいことを特徴とする方法。   A method for producing an extract extract comprising enclosing a dried extract in one or more solvent-permeable containers, immersing the container in a solvent and extracting the extract solids with a solvent, A method characterized in that the volume is smaller than the swelling volume of the encapsulated extract by a solvent. 容器の容積が、封入される被抽出物の膨潤体積の0.6〜0.9倍である、請求項1記載の方法。   The method according to claim 1, wherein the volume of the container is 0.6 to 0.9 times the swelling volume of the encapsulated extract. 被抽出物が植物組織である、請求項1または2記載の方法。   The method according to claim 1 or 2, wherein the extract is plant tissue. 植物組織が薬用人参カルスである、請求項3記載の方法。   The method according to claim 3, wherein the plant tissue is ginseng callus. 請求項1〜4のいずれか1項に記載の方法により得られるエキス抽出液を濃縮することを特徴とする、エキス固形分濃縮物の製造方法。   A method for producing an extract solids concentrate, comprising concentrating an extract extract obtained by the method according to any one of claims 1 to 4.
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