JP6151082B2 - Extraction and production method of plant essential oil - Google Patents

Extraction and production method of plant essential oil Download PDF

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JP6151082B2
JP6151082B2 JP2013094746A JP2013094746A JP6151082B2 JP 6151082 B2 JP6151082 B2 JP 6151082B2 JP 2013094746 A JP2013094746 A JP 2013094746A JP 2013094746 A JP2013094746 A JP 2013094746A JP 6151082 B2 JP6151082 B2 JP 6151082B2
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星野 宗広
宗広 星野
雅裕 田中
雅裕 田中
新 高水
新 高水
卓也 末次
卓也 末次
順弘 川本
順弘 川本
理斗 佐々木
理斗 佐々木
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株式会社 アスキー
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Description

本発明は、植物精油の抽出・製造方法等に関する。詳細には、柑橘類果実・果皮や野菜などの植物体からの効率的な精油抽出・製造方法及び植物エキス抽出・製造方法に関する。   The present invention relates to a method for extracting and producing a plant essential oil. More specifically, the present invention relates to an efficient essential oil extraction / manufacturing method and a plant extract extraction / manufacturing method from plants such as citrus fruits, pericarp and vegetables.

植物由来の精油(エッセンシャルオイル)は、含有する揮発性芳香成分(テルペン類、芳香族化合物など)が特徴的であるため、食品原料(食品香料)としてだけでなく化粧品原料やアロマオイル原料などにも多様されている。また、多くの薬理作用(リラックス効果など)も知られており、今後も様々な用途が広がっていくと予想されている。   Plant-derived essential oils (essential oils) are characterized by the volatile aromatic components they contain (terpenes, aromatic compounds, etc.), so they are not only used as food ingredients (food fragrances) but also as cosmetic ingredients and aroma oil ingredients. It is diverse. Many pharmacological actions (relaxation effects, etc.) are also known, and various uses are expected to expand in the future.

この植物由来の精油を抽出・製造する方法としては、従来より水蒸気蒸留法(特許文献1)、減圧蒸留法(特許文献2)、超臨界抽出法(特許文献3)、溶剤抽出法などが用いられている。しかし、例えば水蒸気蒸留法や減圧蒸留法は、精油成分回収のために多くの熱エネルギーが必要であり、コスト増や精油品質の劣化の問題から小スケールでの製造でしか適さない。また、超臨界抽出法は、大型設備の設計が難しく、これも仕込み量が少なくコスト増につながるという欠点がある。さらには、溶剤抽出法は、食品用途を考慮すると使用できる溶剤の種類が限られ汎用的ではない。   As a method for extracting and producing this plant-derived essential oil, a steam distillation method (Patent Document 1), a vacuum distillation method (Patent Document 2), a supercritical extraction method (Patent Document 3), a solvent extraction method and the like have been used. It has been. However, for example, the steam distillation method and the vacuum distillation method require a large amount of heat energy for recovering essential oil components, and are only suitable for production on a small scale due to problems of cost increase and deterioration of essential oil quality. In addition, the supercritical extraction method has a drawback that it is difficult to design a large-scale facility, which also leads to an increase in cost due to a small amount of preparation. Furthermore, the solvent extraction method is not versatile because the types of solvents that can be used are limited in consideration of food applications.

このような技術背景の中、植物由来の精油等について、より簡便且つ効率的でコスト負担も少ない、汎用的に用いることができる抽出・製造方法等の開発が当業界において求められていた。   In such a technical background, there has been a need in the art for the development of extraction and production methods that can be used for general purposes and that are simpler, more efficient, less expensive, and more, for essential oils derived from plants.

一方、超高圧水(20〜300MPa程度の吐出圧を有する水流)については従来より知られており、主として高圧洗浄などに用いられている。食品への利用としては、固形食品の効率的且つきれいな切断(特許文献4)や糊状食品の切断(特許文献5)などの通常のカッターや包丁等ではきれいに切断しにくい食品の切断目的に用いられているのが認められるのみであり、植物精油の抽出等に用いた例は見当たらないのが現状である。   On the other hand, ultra-high pressure water (water flow having a discharge pressure of about 20 to 300 MPa) has been conventionally known, and is mainly used for high-pressure cleaning and the like. For food use, it is used for the purpose of cutting food that is difficult to clean with ordinary cutters and knives, such as efficient and clean cutting of solid food (Patent Document 4) and cutting of pasty food (Patent Document 5). However, there are no examples of using it for extraction of plant essential oils.

特開2005−298580号公報JP 2005-298580 A 特開2004−018737号公報JP 2004-018737 A 特開2005−213327号公報JP 2005-213327 A 特開2007−296595号公報JP 2007-296595 A 特開平6−233668号公報JP-A-6-233668

本発明は、植物(例えば柑橘類、野菜など)由来の精油等について、より簡便且つ効率的に抽出・製造する方法を提供することを目的とする。   An object of the present invention is to provide a simpler and more efficient method for extracting and producing essential oils derived from plants (for example, citrus fruits and vegetables).

上記目的を達成するため、本発明者らは鋭意研究の結果、植物体を20MPa以上の超高圧水で流量20〜40L/minの条件で破砕処理し、これを固液分離して得られた液体を遠心分離処理によって精油と植物エキスを分離することにより、非常に簡便且つ効率的に植物由来精油及び植物エキスを得ることができ、また大きなコスト負担もない(特殊な製造機器等の必要がない)ことを見出し、本発明を完成した。   In order to achieve the above object, as a result of intensive studies, the present inventors obtained a plant by crushing the plant with ultrahigh pressure water of 20 MPa or more at a flow rate of 20 to 40 L / min, and solid-liquid separation. By separating the essential oil and the plant extract by centrifugal separation of the liquid, it is possible to obtain a plant-derived essential oil and a plant extract very simply and efficiently, and there is no significant cost burden (the need for special production equipment, etc.) The present invention was completed.

すなわち、本発明の実施形態は次のとおりである。
(1)植物体を吐出圧20MPa以上の超高圧水で流量20〜40L/minの条件で破砕処理し、これを固液分離して得られた液体を遠心分離処理によって精油と植物エキスを分離すること、を特徴とする植物由来精油の製造方法(抽出・製造方法)。
(2)吐出圧50〜100MPa(好ましくは80〜100MPa)の超高圧水で処理すること、を特徴とする(1)に記載の方法。
(3)超高圧水を0.5〜1.0mm径のノズルよりカーテン状に噴射して破砕処理すること、を特徴とする(1)又は(2)に記載の方法。
(4)植物体が、柑橘類の果実及び/又は果皮、野菜類、植物加工残渣(果汁絞り滓、野菜滓など)から選ばれる少なくともひとつであること、を特徴とする(1)〜(3)のいずれか1つに記載の方法。
(5)植物体を1cm未満(例えば0.5〜0.8cm程度)にスライスした状態で破砕処理を行うこと、を特徴とする(1)〜(4)のいずれか1つに記載の方法。
That is, the embodiment of the present invention is as follows.
(1) The plant body is crushed with ultrahigh-pressure water with a discharge pressure of 20 MPa or more under conditions of a flow rate of 20 to 40 L / min, and the liquid obtained by solid-liquid separation is separated into essential oil and plant extract by centrifugation. A method for producing a plant-derived essential oil (extraction / manufacturing method).
(2) The method according to (1), characterized by treating with ultrahigh pressure water having a discharge pressure of 50 to 100 MPa (preferably 80 to 100 MPa).
(3) The method according to (1) or (2), characterized in that ultrahigh pressure water is sprayed in a curtain shape from a nozzle having a diameter of 0.5 to 1.0 mm and crushed.
(4) The plant body is at least one selected from citrus fruits and / or fruit peels, vegetables, and plant processing residues (fruit juice squeezed koji, vegetable koji, etc.) (1) to (3) The method as described in any one of these.
(5) The method according to any one of (1) to (4), wherein the plant body is crushed in a state of being sliced to less than 1 cm (for example, about 0.5 to 0.8 cm). .

(6)植物体を吐出圧20MPa以上の超高圧水で流量20〜40L/minの条件で破砕処理し、これを固液分離して得られた液体を遠心分離処理によって精油と植物エキスを分離すること、を特徴とする植物由来エキスの製造方法(抽出・製造方法)。
(7)吐出圧50〜100MPa(好ましくは80〜100MPa)の超高圧水で処理すること、を特徴とする(6)に記載の方法。
(8)超高圧水を0.5〜1.0mm径のノズルよりカーテン状に噴射して破砕処理すること、を特徴とする(6)又は(7)に記載の方法。
(9)植物体が、柑橘類の果実及び/又は果皮、野菜類、植物加工残渣(果汁絞り滓、野菜滓など)から選ばれる少なくともひとつであること、を特徴とする(6)〜(8)のいずれか1つに記載の方法。
(10)植物体を1cm未満(例えば0.5〜0.8cm程度)にスライスした状態で破砕処理を行うこと、を特徴とする(6)〜(9)のいずれか1つに記載の方法。
(6) The plant body is crushed with ultrahigh pressure water having a discharge pressure of 20 MPa or more under a flow rate of 20 to 40 L / min, and the liquid obtained by solid-liquid separation is separated into essential oil and plant extract by centrifugation. A method for producing a plant-derived extract (extraction / manufacturing method).
(7) The method according to (6), characterized by treating with ultrahigh pressure water having a discharge pressure of 50 to 100 MPa (preferably 80 to 100 MPa).
(8) The method according to (6) or (7), characterized in that ultra high pressure water is sprayed in a curtain form from a nozzle having a diameter of 0.5 to 1.0 mm and crushed.
(9) The plant body is at least one selected from citrus fruits and / or fruit peels, vegetables, and plant processing residues (fruit juice squeezed koji, vegetable koji, etc.) (6) to (8), The method as described in any one of these.
(10) The method according to any one of (6) to (9), wherein the plant body is crushed in a state of being sliced to less than 1 cm (for example, about 0.5 to 0.8 cm). .

本発明によれば、植物体を吐出圧20MPa以上の超高圧水で流量20〜40L/minの条件で破砕処理することで植物体が細胞レベルまで破砕された状態となり、これを固液分離して得られた液体は精油と植物エキスがエマルジョン状態となっているため、これを単に遠心分離処理するだけで簡便且つ効率的に精油及び植物エキスを得ることができる。そして、本発明の方法では、大きな熱が長時間かかる工程がないため、得られる精油及び植物エキスの品質劣化がほとんどないこと、及び、超臨界抽出機などのような特殊な設備を必要とせず仕込み量等の制限がない(大量処理もできコスト負担が少ない)ことも特徴である。   According to the present invention, the plant body is crushed to a cell level by crushing the plant body with ultrahigh pressure water having a discharge pressure of 20 MPa or more at a flow rate of 20 to 40 L / min, and this is solid-liquid separated. In the liquid obtained, the essential oil and the plant extract are in an emulsion state. Therefore, the essential oil and the plant extract can be easily and efficiently obtained simply by centrifugation. In the method of the present invention, since there is no process that takes a large amount of heat for a long time, there is almost no deterioration in the quality of the obtained essential oil and plant extract, and no special equipment such as a supercritical extractor is required. Another feature is that there is no restriction on the amount of preparation (a large amount of processing is possible and the cost burden is low).

本発明では、まず精油及びエキスの抽出原料となるのは植物体である。植物体とは、植物の葉、茎、根、花、実(果実)等のあらゆる部分の少なくとも1以上を意味するが、植物の種類に応じて精油等が多く含まれる部分を適宜選択して使用してよい。なお、本発明においては、柑橘類(ミカン類、オレンジ類、香酸柑橘類、グレープフルーツ類など)の果実及び/又は果皮、野菜類、植物加工残渣(果汁絞り滓、野菜滓など)から選ばれる少なくともひとつを原料とするのが好適である。   In the present invention, the plant is first used as an extraction raw material for essential oils and extracts. The plant body means at least one or more of all parts such as plant leaves, stems, roots, flowers, fruits (fruits), etc., and appropriately select a part containing a lot of essential oils depending on the type of plant. May be used. In the present invention, at least one selected from the fruits and / or peels of citrus fruits (mandarin oranges, oranges, citrus citrus fruits, grapefruits, etc.), vegetables, plant processing residues (fruit juice squeezed strawberries, vegetable strawberries, etc.). Is preferably used as a raw material.

そして、抽出前の前処理として、原料となる植物体を1cm未満(例えば0.5〜0.8cm程度)にスライスした状態としておくことが好ましい。これにより、後の超高圧水による破砕処理がより効率的且つ効果的となるものであるが、原料の種類や状態に応じてスライスの有無を適宜選択すれば良い。   And it is preferable to make it the state which sliced the plant body used as a raw material to less than 1 cm (for example, about 0.5-0.8 cm) as pre-processing before extraction. As a result, the subsequent crushing treatment with ultra-high pressure water becomes more efficient and effective, but the presence or absence of the slice may be appropriately selected according to the type and state of the raw material.

次に、上述のようにして調製した抽出原料を超高圧水により破砕処理する。超高圧水は、特定の吐出圧を有する水流であるが、本発明では吐出圧力が20MPa以上、例えば20〜300MPa程度であることが必要であり、好ましい圧力範囲は50〜100MPa、さらに好ましくは80〜100MPaである。また、流量は20〜40L/minが好ましく、設定圧力に応じてこの範囲で調整すれば良い。   Next, the extraction raw material prepared as described above is crushed with ultra-high pressure water. The ultra-high pressure water is a water stream having a specific discharge pressure, but in the present invention, the discharge pressure needs to be 20 MPa or more, for example, about 20 to 300 MPa, and a preferable pressure range is 50 to 100 MPa, more preferably 80. ~ 100 MPa. The flow rate is preferably 20 to 40 L / min, and may be adjusted within this range according to the set pressure.

超高圧水を吐出するノズルについては、限定はされないが、その効果を最大限発揮させるためにノズル径が0.5〜1.0mmであることが望ましい。なお、ノズルの径が大きすぎる場合、所望する圧力設定や効果が得られない場合があり好ましくない。また、ノズルの形状は丸型線状であるのが好適である。そして、ノズルからの植物体への超高圧水噴射方法は、破砕効率等を考慮すると植物体に対してカーテン状(波形状)に噴射されるようにノズル又は植物体を動かして行うことが望ましいが、ノズル形状や噴射方法は必ずしもこれらに限定されるものではない。   The nozzle for discharging the ultrahigh pressure water is not limited, but the nozzle diameter is desirably 0.5 to 1.0 mm in order to maximize the effect. If the nozzle diameter is too large, the desired pressure setting and effect may not be obtained, which is not preferable. Moreover, it is suitable that the shape of the nozzle is a round linear shape. Then, it is desirable that the ultrahigh pressure water injection method from the nozzle to the plant body is performed by moving the nozzle or the plant body so that the plant body is sprayed in a curtain shape (wave shape) in consideration of crushing efficiency and the like. However, the nozzle shape and the injection method are not necessarily limited to these.

このようにして設定した超高圧水をコンベア上等で植物体に噴射して、植物体を細胞レベルまで破砕処理する。この破砕処理においては、植物体の破砕と植物体(細胞)からの精油及びエキスの抽出を同時に行うこととなる。したがって、本発明においては、当該破砕処理以外の抽出工程(水蒸気蒸留工程など)を要しない。そして、破砕処理後の植物体破砕物及び水(植物体由来のもの及び超高圧水由来のもの)は、全て回収できるようなシステム又は製造ライン設計としておく。   The ultrahigh pressure water set in this way is sprayed onto the plant body on a conveyor or the like, and the plant body is crushed to the cell level. In this crushing treatment, crushing of the plant body and extraction of the essential oil and extract from the plant body (cell) are performed simultaneously. Therefore, in this invention, extraction processes (steam distillation process etc.) other than the said crushing process are not required. And the plant crushed material and water (the thing derived from a plant body and the thing derived from super-high pressure water) after a crushing process are set as the system or production line design which can collect | recover all.

そして、破砕処理後に回収された破砕物含有処理液は、メッシュ等により固液分離して不溶物を除去する。不溶物を除去した液体は、精油成分と植物エキスがエマルジョン状態(乳化状態)となっているため、これを遠心分離処理によって油層と水層に分離する。遠心分離条件は、液体の状態により適宜設定すれば良いが、例えば1,000〜3000×gで5〜20分間程度の条件が例示される。   And the crushed material containing processing liquid collect | recovered after the crushing process is solid-liquid separated with a mesh etc., and an insoluble matter is removed. Since the essential oil component and the plant extract are in an emulsion state (emulsified state), the liquid from which the insoluble matter has been removed is separated into an oil layer and an aqueous layer by centrifugation. Centrifugation conditions may be set as appropriate depending on the state of the liquid, and examples include conditions of 1,000 to 3000 × g for about 5 to 20 minutes.

このようにして得られた油層(精油)と水層(植物エキス)は、そのまま最終製品としても良いし、必要があればフィルターろ過等の清澄化処理や濃縮処理、殺菌処理などを行って最終製品としても良い。また、これらは更なる有用成分(例えば植物ポリフェノールなど)の抽出・精製原料とすることも可能である。   The oil layer (essential oil) and the aqueous layer (plant extract) thus obtained may be used as final products as they are, and if necessary, they are finally subjected to clarification treatment such as filter filtration, concentration treatment, sterilization treatment, etc. Good as a product. These can also be used as raw materials for extraction and purification of further useful components (for example, plant polyphenols).

このようにして、植物体に超高圧処理を行うことにより、加熱加圧抽出に代表されるような過酷な条件を得ずとも簡便且つ効率的に精油(エッセンシャルオイル)及び植物エキスを取得することができ、得られた精油及び植物エキスは高品質でありながらコスト負担が少ないものである。   In this way, by performing an ultra-high pressure treatment on a plant body, it is possible to easily and efficiently obtain an essential oil (essential oil) and a plant extract without obtaining harsh conditions as typified by heat and pressure extraction. The essential oils and plant extracts obtained are of high quality and low cost.

以下、本発明の実施例について述べるが、本発明はこれらの実施例のみに限定されるものではなく、本発明の技術的思想内においてこれらの様々な変形が可能である。   Examples of the present invention will be described below, but the present invention is not limited to these examples, and various modifications can be made within the technical idea of the present invention.

(みかんからの精油等抽出)
みかん(温州みかん)の超高圧水処理により精油等を抽出できることを確認するため、以下の試験を実施した。
(Extraction of essential oils from mandarin oranges)
In order to confirm that essential oils and the like can be extracted by treating the mandarin orange (Wanzhou mandarin orange) with ultra-high pressure water, the following tests were conducted.

温州みかんの果実(果皮を含む)を概ね1cm未満となるようにスライスし、これを吐出圧として20MPa、40MPa、50MPa、80MPa、100MPaに設定した5種類の超高圧水を用いていずれも流量30L/minでそれぞれ破砕処理を行った。なお、超高圧水は、1mm径の丸型線状ノズルから植物体(スライスみかん)に向けてカーテン状に噴射した。得られた破砕処理液はメッシュで濾過して固液分離し、液体部を遠心分離(1,500×g、10分間)して油層と水層を分離した。   Sliced Wenzhou mandarin fruit (including pericarp) to be less than 1 cm, and using 5 types of ultra-high pressure water set to 20MPa, 40MPa, 50MPa, 80MPa and 100MPa as the discharge pressure, the flow rate is 30L. Each crushing process was performed at / min. The ultra-high pressure water was sprayed from a 1 mm diameter round linear nozzle toward the plant body (sliced mandarin orange) in a curtain shape. The obtained crushed liquid was filtered through a mesh for solid-liquid separation, and the liquid part was centrifuged (1,500 × g, 10 minutes) to separate an oil layer and an aqueous layer.

この結果、各処理のいずれにおいても高品質のミカンフレーバーオイル(油層)及びミカンエキス(水層)を得ることができた。特に、50MPa以上(50MPa、80MPa、100MPa)の吐出圧の超高圧水で処理することにより、植物体(みかん)が極めて短時間で非常に細かく粉砕され、非常に高品質の精油及びエキスを得られることが明らかとなった。   As a result, high quality mandarin flavor oil (oil layer) and citrus extract (water layer) could be obtained in any of the treatments. In particular, by treating with ultra-high pressure water having a discharge pressure of 50 MPa or more (50 MPa, 80 MPa, 100 MPa), the plant body (mandarin orange) is crushed very finely in a very short time, and very high quality essential oils and extracts are obtained. It became clear that

(人参からの精油等抽出)
人参の超高圧水処理により精油等を抽出できることを確認するため、以下の試験を実施した。
(Extract essential oil from carrot)
In order to confirm that essential oils and the like can be extracted by carrot ultra-high pressure water treatment, the following tests were conducted.

洗浄した人参の根部(皮を含む)を概ね1cm未満となるようにスライスし、これを吐出圧として20MPa、40MPa、50MPa、80MPa、100MPaに設定した5種類の超高圧水を用いていずれも流量30L/minでそれぞれ破砕処理を行った。なお、超高圧水は、1mm径の丸型線状ノズルから植物体(スライス人参)に向けてカーテン状に噴射した。得られた破砕処理液はメッシュで濾過して固液分離し、液体部を遠心分離(1,500×g、10分間)して油層と水層を分離した。   Sliced carrot roots (including skin) to be less than 1 cm, and using 5 types of ultra-high pressure water with discharge pressure set to 20 MPa, 40 MPa, 50 MPa, 80 MPa, and 100 MPa. Each crushing process was performed at 30 L / min. The ultra-high pressure water was sprayed from a 1 mm diameter round linear nozzle toward the plant body (sliced carrot) in a curtain shape. The obtained crushed liquid was filtered through a mesh for solid-liquid separation, and the liquid part was centrifuged (1,500 × g, 10 minutes) to separate an oil layer and an aqueous layer.

この結果、各処理のいずれにおいても高品質のニンジンフレーバーオイル(油層)及びニンジンエキス(水層)を得ることができた。特に、50MPa以上(50MPa、80MPa、100MPa)の吐出圧の超高圧水で処理することにより、植物体(人参)が極めて短時間で非常に細かく粉砕され、非常に高品質の精油及びエキスを得られることが明らかとなった。   As a result, high quality carrot flavor oil (oil layer) and carrot extract (water layer) could be obtained in any of the treatments. In particular, by treating with ultra-high pressure water having a discharge pressure of 50 MPa or more (50 MPa, 80 MPa, 100 MPa), the plant body (carrot) is very finely pulverized in a very short time, and very high quality essential oils and extracts are obtained. It became clear that

本発明を要約すれば、以下の通りである。   The present invention is summarized as follows.

本発明は、植物(例えば柑橘類、野菜など)由来の精油等について、より簡便且つ効率的に抽出・製造する方法を提供することを目的とする。   An object of the present invention is to provide a simpler and more efficient method for extracting and producing essential oils derived from plants (for example, citrus fruits and vegetables).

そして、植物体を吐出圧20MPa以上(例えば50〜100MPa)の超高圧水で流量20〜40L/minの条件で破砕処理し、これを固液分離して得られた液体を遠心分離処理によって精油と植物エキスを分離することにより、非常に簡便且つ効率的に植物由来精油及び植物エキスを得ることができ、特殊な製造機器など必要なく大きなコスト負担もない。   The plant body is crushed with ultrahigh pressure water having a discharge pressure of 20 MPa or more (for example, 50 to 100 MPa) at a flow rate of 20 to 40 L / min. By separating plant extracts from plant extracts, plant-derived essential oils and plant extracts can be obtained very simply and efficiently, no special production equipment is required, and there is no large cost burden.

Claims (4)

1cm未満にスライスした柑橘類の果実及び果皮、1cm未満にスライスした野菜類、柑橘類果汁絞り滓、野菜滓から選ばれる少なくともひとつを吐出圧50〜100MPaの超高圧水で流量20〜40L/minの条件で0.5〜1.0mm径のノズルより噴射して破砕処理し、これを固液分離して得られた液体を遠心分離処理によって精油と植物エキスを分離すること、を特徴とする植物由来精油の製造方法。 Citrus fruits and fruit skins sliced to less than 1 cm, at least one selected from vegetables sliced to less than 1 cm, citrus fruit juice squeezed koji , and vegetable koji with ultra high pressure water at a discharge pressure of 50 to 100 MPa and a flow rate of 20 to 40 L / min The liquid is obtained by spraying from a nozzle having a diameter of 0.5 to 1.0 mm and crushing, and separating the liquid into solid and liquid to separate the essential oil and the plant extract by centrifugal separation. Essential oil production method. 超高圧水をノズルよりカーテン状に噴射して破砕処理すること、を特徴とする請求項1に記載の方法。     The method according to claim 1, wherein ultra high pressure water is sprayed in a curtain form from a nozzle and crushed. 1cm未満にスライスした柑橘類の果実及び果皮、1cm未満にスライスした野菜類、柑橘類果汁絞り滓、野菜滓から選ばれる少なくともひとつを吐出圧50〜100MPaの超高圧水で流量20〜40L/minの条件で0.5〜1.0mm径のノズルより噴射して破砕処理し、これを固液分離して得られた液体を遠心分離処理によって精油と植物エキスを分離すること、を特徴とする植物由来エキスの製造方法。 Citrus fruits and fruit skins sliced to less than 1 cm, at least one selected from vegetables sliced to less than 1 cm, citrus fruit juice squeezed koji , and vegetable koji with ultra high pressure water at a discharge pressure of 50 to 100 MPa and a flow rate of 20 to 40 L / min The liquid is obtained by spraying from a nozzle having a diameter of 0.5 to 1.0 mm and crushing, and separating the liquid into solid and liquid to separate the essential oil and the plant extract by centrifugal separation. Extract manufacturing method. 超高圧水をノズルよりカーテン状に噴射して破砕処理すること、を特徴とする請求項3に記載の方法。4. The method according to claim 3, wherein ultra high pressure water is sprayed in a curtain form from a nozzle and crushed.
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