JPH10316991A - Preparation of natural essential oil which does not contain psoralen compound - Google Patents

Preparation of natural essential oil which does not contain psoralen compound

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Publication number
JPH10316991A
JPH10316991A JP13917697A JP13917697A JPH10316991A JP H10316991 A JPH10316991 A JP H10316991A JP 13917697 A JP13917697 A JP 13917697A JP 13917697 A JP13917697 A JP 13917697A JP H10316991 A JPH10316991 A JP H10316991A
Authority
JP
Japan
Prior art keywords
essential oil
carbon dioxide
psoralen
psoralens
natural essential
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.)
Pending
Application number
JP13917697A
Other languages
Japanese (ja)
Inventor
Kenichi Awano
健一 粟野
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
T Hasegawa Co Ltd
Original Assignee
T Hasegawa Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by T Hasegawa Co Ltd filed Critical T Hasegawa Co Ltd
Priority to JP13917697A priority Critical patent/JPH10316991A/en
Publication of JPH10316991A publication Critical patent/JPH10316991A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To remove psoralen compds. from a natural essential oil contg. the same industrially easily without adversely affeting the yield, the perfume component balance of the oil, etc., by fractionating the psoralen compds. with carbon dioxide in the subcritical or supercritical state as a fluid and with a supercritical carbon dioxide extraction column chromatograph apparatus filled with a porous polymeric resin. SOLUTION: An extraction container/separation column 5 is filled with a porous polymeric resin having a specific surface area of 300-700 m<2> /g, a microproe vol. of 0.7-1.1 ml/g, and a micropore radius of 50-1,300 Å. Then, carbon dioxide in a subcritical or supercritical state at 31 deg.C or lower under a pressure of 75 kg/cm<2> or higher is supplied together with a natural essential oil contg. psoralen compds. from a bomb 1 through a spare coil 2, an indicator 3, and a six-way valve 6 to the separation column in order to cause the porous polymeric resin to adsorb the psoralen compds. to fractionate and remove them. The essential oil dissolved in carbon dioxide and contg. no psoralen compd. is separated from carbon dioxide in the gas-liq. separation column 5.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、皮膚に有害作用を
与える原因となるプソラレン類を含有する天然精油から
該原因物質を、操作上のトラブルや副反応の生起などの
欠陥を伴うおそれなしに、天然精油の香気、その成分バ
ランス、収量などに悪影響を与えることなしに、工業的
に容易な手段で有利に除去でき、しかして品質の優れた
実質的にプソラレン類を含有しない天然精油の製法に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for removing a causative substance from a natural essential oil containing psoralens, which may cause a harmful effect on the skin, without causing any troubles such as operational troubles and side reactions. A method for producing a natural essential oil which is advantageously free of industrially-friendly psoralens and which can be advantageously removed by industrially easy means without adversely affecting the aroma of natural essential oil, its component balance, yield, etc. About.

【0002】更に詳しくは、本発明はプソラレン類含有
天然精油を、亜臨界又は超臨界状態の二酸化炭素を流体
として、多孔性重合樹脂を充填した超臨界二酸化炭素抽
出カラムクロマト装置を用いて、該天然精油中のプソラ
レン類を分画せしめることを特徴とする、プソラレン類
を実質的に含有しない天然精油の製造法に関する。
More specifically, the present invention relates to a method for producing a psoralen-containing natural essential oil using a supercritical carbon dioxide extraction column chromatograph filled with a porous polymer resin using subcritical or supercritical carbon dioxide as a fluid. The present invention relates to a method for producing a natural essential oil substantially free of psoralens, which comprises fractionating psoralens in a natural essential oil.

【0003】[0003]

【従来の技術】天然精油は各種の香粧品用香料として、
例えば、クリーム、化粧水、ローションその他の基礎化
粧料;口紅、白粉などの化粧料;ポマード、ヘアクリー
ム、ヘアトニックその他の整髪料等に広く利用されてい
る。
2. Description of the Related Art Natural essential oils are used as various fragrances for cosmetics.
For example, they are widely used in creams, lotions, lotions and other basic cosmetics; lipsticks, white powders and other cosmetics; pomades, hair creams, hair tonics and other hair styling products.

【0004】しかしながら、天然精油中に含有されてい
るクマリン核をもつプソラレン類が光毒作用を呈し、例
えば、皮膚炎の原因となることが知られている。このよ
うな炎症の原因について、THOMAS B・FITZPATRICK;Sunl
ight and Man(University of TOKYO PRESS.1974)に
は、このような光毒作用の原因は、天然精油中に含有さ
れるクマリン核をもつ化合物、例えば、プソラレン、4
−メチルプソラレン、4,4’−ジメチルプソラレン、
4,5’−ジメチルプソラレン、4’,8−ジメチルプ
ソラレン、4,5’,8−トリメチルプソラレン、5,
7−ジメトキシクマリン、8−メトキシプソラレン、5
−メトキシプソラレンで示されるようなプソラレン類
が、上記原因物質となることを記載している。そこで、
天然精油の香気、色調、成分バランス等に悪影響を与え
ることなくこれら光毒性物質のみを精油から除去するこ
とが望まれている。
[0004] However, it is known that psoralens having a coumarin nucleus contained in natural essential oils exhibit phototoxic effects and cause, for example, dermatitis. About the cause of such inflammation, THOMAS B ・ FITZPATRICK; Sunl
According to ight and Man (University of TOKYO PRESS. 1974), such phototoxic effects are caused by compounds having a coumarin nucleus contained in natural essential oils such as psoralen,
-Methylpsoralen, 4,4′-dimethylpsoralen,
4,5′-dimethylpsoralen, 4 ′, 8-dimethylpsoralen, 4,5 ′, 8-trimethylpsoralen, 5,
7-dimethoxycoumarin, 8-methoxypsoralen, 5
It is described that psoralens represented by -methoxypsoralen are the causative substances. Therefore,
It is desired to remove only these phototoxic substances from essential oils without adversely affecting the aroma, color tone, component balance, etc. of the natural essential oils.

【0005】従来、このような皮膚障害の原因となる光
毒性物質を除去する方法として、天然精油の一種である
ベルガモット精油を減圧蒸留して留出精油を得、一方、
蒸留残渣をアルコール性アルカリで冷時加水分解して、
プソラレン類をその加水分解物のアルカリ塩の形に転化
させることにより除去し、残った中性油を上記留出精油
と合することにより皮膚に刺激を与えないベルガモット
精油を製造する方法が提案されている(特公昭35−1
5363号公報)
Conventionally, as a method for removing such phototoxic substances causing skin damage, bergamot essential oil, a kind of natural essential oil, is distilled under reduced pressure to obtain a distillate essential oil.
The distillation residue is cold-hydrolyzed with alcoholic alkali,
A method for producing bergamot essential oil which does not irritate the skin by removing psoralens by converting the hydrolyzate into an alkali salt form and combining the remaining neutral oil with the distillate essential oil has been proposed. (35-1)
No. 5363)

【0006】また、天然精油の一種であるレモン油を、
減圧蒸留を行って留出油を得、一方、蒸留残渣に無極性
溶媒を加え、フロクマリン類を析出させて除去し、さら
に残存するフロクマリン類を無機吸着剤(アルミナ、シ
リカゲル)に吸着せしめて除去した後、溶媒を除いた油
を、前記留出油と合して光毒性を有しないレモン油を製
造する方法が知られている(特開昭56−70096号
公報)。また、レモン油の代わりにベルガモット油を用
い、同様の処理工程によりベルガプテンを除去するベル
ガモット油の精製方法も提案されている(特開昭58−
127797号公報)。
[0006] Lemon oil, a kind of natural essential oil,
A distillate is obtained by vacuum distillation, while a non-polar solvent is added to the distillation residue to remove and remove the flocoumarins, and the remaining flocoumarins are absorbed and removed by an inorganic adsorbent (alumina, silica gel). After that, a method is known in which oil excluding the solvent is combined with the distillate oil to produce lemon oil having no phototoxicity (JP-A-56-70096). A method of purifying bergamot oil using bergamot oil instead of lemon oil and removing bergapten by the same treatment step has also been proposed (Japanese Patent Application Laid-Open No. 58-1983).
127797).

【0007】更に、他の提案として、プソラレン類及び
(または)クマリン類を含有する天然精油を減圧蒸留し
て留出精油と残留精油とに分け、残留精油を水混和性有
機溶媒に溶解し、得られる溶液に亜硫酸アルカリ金属塩
の水溶液を加えて混合後有機溶媒層を分取して溶媒を留
去し、得られる残渣を上記留出精油と合してプソラレン
類及びクマリン類を含有しない天然精油を製造する方法
が知られている(特開昭57−5794号公報)。
Further, as another proposal, a natural essential oil containing psoralens and / or coumarins is distilled under reduced pressure to distill essential oil and residual essential oil, and the residual essential oil is dissolved in a water-miscible organic solvent, An aqueous solution of an alkali metal sulfite is added to the obtained solution, and after mixing, the organic solvent layer is separated and the solvent is distilled off.The obtained residue is combined with the above-mentioned distillate essential oil to obtain a natural solution free of psoralens and coumarins. A method for producing an essential oil is known (JP-A-57-5794).

【0008】或いは、プソラレン類含有天然精油を、蒸
留処理前に活性白土で接触処理してプソラレン類を吸着
除去する、プソラレン類を実質的に含有しない天然精油
の製法(特開昭59−142297号公報)、また、オ
レンジ花精油を蒸留した残渣に無極性溶媒を加え、溶解
油部を高分子吸着剤充填カラムクロマトでプソラレン類
を吸着除去する光毒性オレンジ花精油の製法(特公平8
−16232号公報)も提案されている。
Alternatively, a method for producing a natural essential oil substantially free of psoralens by subjecting a psoralen-containing natural essential oil to contact treatment with activated clay before distillation to adsorb and remove the psoralens (Japanese Patent Application Laid-Open No. 59-142297) And a non-polar solvent is added to the residue obtained by distilling orange flower essential oil, and the dissolved oil portion is adsorbed and removed by column chromatography packed with a polymer adsorbent to remove psoralens.
No. 16232) has also been proposed.

【0009】上記の提案が天然精油を蒸留、溶媒抽出、
吸着剤処理によりプソラレン類を除去する方法に対し、
超臨界炭酸ガスを抽剤としてシリカゲルを充填したカラ
ムクロマトによりプソラレン類を分画除去する方法が提
案されている[J.Chromatogr.1990,505,237、及び、J.S
upercrit.Fluids,7(3),177-183,(1994)]。
[0009] The above proposal is to distill natural essential oil, solvent extraction,
For the method of removing psoralens by adsorbent treatment,
A method for fractionating and removing psoralens by column chromatography packed with silica gel using supercritical carbon dioxide as an extractant has been proposed [J. Chromatogr. 1990, 505 , 237, and JS.
upercrit. Fluids, 7 (3), 177-183, (1994)].

【0010】[0010]

【発明が解決しようとする課題】しかしながら、天然精
油を蒸留、溶媒抽出、吸着剤処理によりプソラレン類を
除去する方法は、プソラレン類のみを除去して元の香気
成分のバランスをくずさず再現しようとしているにもか
かわらず、蒸留の際の加熱による化学変化、或いは使用
した溶媒の回収時における香気成分の損失などにより必
ずしも満足できる再現はなされていない。
However, the method of removing psoralens by distillation, solvent extraction, and adsorbent treatment of natural essential oils is intended to remove only psoralens and reproduce the original aroma components without breaking the balance. Nevertheless, satisfactory reproduction has not always been achieved due to a chemical change due to heating during distillation, or a loss of aroma components during recovery of the used solvent.

【0011】また、超臨界状態の二酸化炭素を抽剤とし
てシリカゲルを充填したカラムクロマトによりプソラレ
ン類を分画除去する方法は、上記の蒸留、溶媒抽出によ
る方法に比較してより好ましい方法ではあるが、プソラ
レン類を溶出させない条件下では、アルコール、アルデ
ヒドなどの極性を有する香気成分はシリカゲルにかなり
強固に吸着されるため溶出が不充分であり、元の香気成
分の再現の点からは香気的バランスに問題があり不満足
である。従って、プソラレン類を実質的に含有しない精
油を得ようとすると、香気的に不満足なものとなり、一
方、香気を重視するとプソラレン類の除去が不充分とな
って、香粧品用香料としての使用が制約されることな
ど、プソラレン類の除去方法については更なる改良が求
められていた。
A method for fractionating and removing psoralens by column chromatography packed with silica gel using carbon dioxide in a supercritical state as an extractant is a more preferable method than the above-mentioned method by distillation and solvent extraction. Under conditions that do not elute psoralens, polar fragrance components such as alcohols and aldehydes are adsorbed to silica gel quite strongly, so their dissolution is insufficient, and the fragrance balance from the viewpoint of reproducing the original fragrance components Have problems and are unsatisfactory. Therefore, if an attempt is made to obtain an essential oil containing substantially no psoralens, the fragrance is unsatisfactory. On the other hand, if the fragrance is emphasized, the removal of the psoralens becomes insufficient, so that the use as a fragrance for cosmetics becomes difficult. There has been a demand for further improvements in the method of removing psoralens, such as being restricted.

【0012】[0012]

【課題を解決するための手段】そこで本発明者らは、こ
れら欠点を改善すべく鋭意研究を行なってきた。その結
果、プソラレン類を含有する天然精油を、亜臨界又は超
臨界状態の二酸化炭素を流体として、多孔性重合樹脂を
充填した超臨界二酸化炭素抽出カラムクロマト装置を用
い、該天然精油中のプソラレン類を分画することによ
り、実質的にプソラレン類を含有しない天然精油の製造
法を見出し本発明を完成した。
The present inventors have intensively studied to improve these disadvantages. As a result, the natural essential oil containing psoralens, using subcritical or supercritical carbon dioxide as a fluid, using a supercritical carbon dioxide extraction column chromatography apparatus filled with a porous polymer resin, the psoralens in the natural essential oils The present inventors have found a method for producing a natural essential oil substantially free of psoralens and completed the present invention.

【0013】従って、本発明の目的は、従来から行われ
ている、蒸留と有機溶媒抽出操作等によるプソラレン類
の除去方法や、シリカゲルを吸着剤とした超臨界状態の
二酸化炭素による除去方法では到底得られない、変質等
の劣化もなく、天然精油の香気成分バランスそのままの
実質的にプソラレン類を含有しない天然精油の製造法、
ならびに光毒性のない香粧品用香料を提供するにある。
Accordingly, an object of the present invention is to provide a method for removing psoralens by distillation and organic solvent extraction, or a method for removing carbon dioxide in a supercritical state using silica gel as an adsorbent. A method for producing a natural essential oil substantially free of psoralens, which is not obtained, has no deterioration such as deterioration, and maintains the flavor component balance of the natural essential oil as it is,
Another object of the present invention is to provide a cosmetic fragrance having no phototoxicity.

【0014】[0014]

【発明の実施の形態】本発明によれば、プソラレン類を
含有する天然精油を、亜臨界又は超臨界状態の二酸化炭
素を流体とした、多孔性重合樹脂を充填した超臨界二酸
化炭素抽出カラムクロマト装置に注入し、該天然精油中
のプソラレン類を多孔性重合樹脂に吸着させて分画除去
することができる。亜臨界又は超臨界状態の二酸化炭素
で溶出されたプソラレン類を含有しない精油は、気−液
分離カラム内で二酸化炭素と分離され、もとの精油の香
気バランスを維持している。
DESCRIPTION OF THE PREFERRED EMBODIMENTS According to the present invention, a supercritical carbon dioxide extraction column chromatograph filled with a porous polymer resin using a natural oil containing psoralens as a fluid in subcritical or supercritical carbon dioxide is used. The psoralens in the natural essential oil can be adsorbed to the porous polymer resin and fractionated and removed. The psoralen-free essential oil eluted with subcritical or supercritical carbon dioxide is separated from carbon dioxide in a gas-liquid separation column, and maintains the aroma balance of the original essential oil.

【0015】本発明において用いるプソラレン含有天然
精油としては、例えば、ベルガモット油、レモン油、オ
レンジ油、グレープフルーツ油、ペチグレン油、ライム
油、マンダリン油、ベルベナ油、アンゲリカ油などの天
然精油を例示できる。
Examples of the psoralen-containing natural essential oil used in the present invention include natural essential oils such as bergamot oil, lemon oil, orange oil, grapefruit oil, petiglen oil, lime oil, mandarin oil, verbena oil and angelica oil.

【0016】本発明で使用する超臨界二酸化炭素抽出カ
ラムクロマト装置としては、超臨界二酸化炭素供給部、
試料注入部、抽出−クロマト分離部、気−液分離部より
なる装置であれば如何なる装置でも使用可能である。図
1は、その1例である超臨界二酸化炭素抽出カラムクロ
マト装置の概略構成図である。
The supercritical carbon dioxide extraction column chromatography apparatus used in the present invention includes a supercritical carbon dioxide supply unit,
Any device can be used as long as the device includes a sample injection unit, an extraction-chromatography separation unit, and a gas-liquid separation unit. FIG. 1 is a schematic configuration diagram of an example of a supercritical carbon dioxide extraction column chromatography apparatus.

【0017】本発明で用いられる亜臨界又は超臨界状態
の二酸化炭素としては、温度が31℃以下、圧力が75
Kg/cm2以上の亜臨界状態の二酸化炭素の利用が可
能であるが、好ましくは、温度が20℃〜30℃、圧力
が75Kg/cm2〜120Kg/cm2の亜臨界状態の
二酸化炭素を例示することができる。また、超臨界状態
の二酸化炭素としては、温度が31℃以上、圧力が75
Kg/cm2以上の超臨界状態の二酸化炭素の利用が可
能であるが、好ましくは、温度が30℃〜50℃、圧力
が75Kg/cm2〜100Kg/cm2の超臨界状態の
二酸化炭素を例示することができる。上記の亜臨界又は
超臨界状態の二酸化炭素以外ではプソラレン類が溶出す
る危険性があり好ましくない場合がある。
The subcritical or supercritical carbon dioxide used in the present invention has a temperature of 31 ° C. or less and a pressure of 75 ° C.
Kg / cm 2 or more are possible the use of carbon dioxide in a subcritical state, preferably, the temperature is 20 ° C. to 30 ° C., the pressure of carbon dioxide in the subcritical state of 75Kg / cm 2 ~120Kg / cm 2 Examples can be given. The supercritical carbon dioxide has a temperature of 31 ° C. or more and a pressure of 75 ° C.
Kg / cm 2 or more are possible the use of supercritical carbon dioxide, preferably, the temperature is 30 ° C. to 50 ° C., the pressure of carbon dioxide in the supercritical state of 75Kg / cm 2 ~100Kg / cm 2 Examples can be given. Other than the above-described subcritical or supercritical carbon dioxide, there is a risk that psoralens may elute, which is not preferable.

【0018】また、本発明で使用する多孔性吸着樹脂と
しては、スチレン・ジビニルベンゼ系又はメタクリル酸
エステル系多孔性重合樹脂(以下単に合成吸着剤と称す
ることがある)を挙げることができる。スチレン・ジビ
ニルベンゼ系多孔性重合樹脂吸着剤としては、例えば、
比表面積約300〜約700m2/g;細孔容積約0.
7〜約1.1ml/g;細孔半径約50〜約1300Å
の範囲の物性を有する樹脂を挙げることができる。この
ような合成吸着剤は市場で容易に入手することができ、
例えば、ダイヤイオンHP10、同HP20、同HP3
0、同HP40、同HP50、同SP206、同SP2
07(以上三菱化学社製);アンバーライトXAD−
2、同XAD−4(以上Rohm&Haas社製);日
立ゲル#3010、同#3011、同#3019(以上
日立化成社製)等を挙げることができる。
Further, as the porous adsorption resin used in the present invention, a styrene / divinylbenze-based or methacrylate-based porous polymer resin (hereinafter sometimes simply referred to as a synthetic adsorbent) can be exemplified. As a styrene-divinylbenze-based porous polymer resin adsorbent, for example,
Specific surface area of about 300 to about 700 m 2 / g;
7 to about 1.1 ml / g; pore radius about 50 to about 1300 °
Resins having physical properties in the range described above can be mentioned. Such synthetic adsorbents are readily available on the market,
For example, Diaion HP10, HP20, HP3
0, same HP40, same HP50, same SP206, same SP2
07 (all manufactured by Mitsubishi Chemical Corporation); Amberlite XAD-
2. XAD-4 (above, manufactured by Rohm &Haas); Hitachi Gel # 3010, # 3011, # 3019 (above, manufactured by Hitachi Chemical) and the like.

【0019】また、メタクリル酸エステル系多孔性重合
樹脂吸着剤としては、上記のスチレン・ジビニルベンゼ
系多孔性重合樹脂吸着剤と同程度の比表面積、細孔容積
及び細孔半径を有する樹脂を例示することができ、例え
ば、ダイヤイオンHP1MG、同HP2MG(三菱化学
社製);アンバーライトXAD−7、同XAD−8i
(以上Rohm&Haas社製)等を挙げることができ
る。
Examples of the methacrylate-based porous polymer resin adsorbent include resins having the same specific surface area, pore volume and pore radius as those of the styrene / divinylbenze-based porous polymer resin adsorbent described above. For example, Diaion HP1MG and Diaion HP2MG (manufactured by Mitsubishi Chemical Corporation); Amberlite XAD-7, XAD-8i
(All manufactured by Rohm & Haas).

【0020】上記した如き多孔性重合樹脂吸着剤の使用
量としては、プソラレン類含有天然精油1重量部に対し
て約2〜約10重量部、好ましくは約3〜約6重量部の
使用量を挙げることができる。
The amount of the porous polymer resin adsorbent as described above may be about 2 to about 10 parts by weight, preferably about 3 to about 6 parts by weight, per 1 part by weight of the psoralen-containing natural essential oil. Can be mentioned.

【0021】本発明方法の好ましい一実施態様によれ
ば、例えば、前記例示の如き天然精油の約1gをインジ
ェクターでアンバーライトXAD−7が充填されたカラ
ムに注入し、温度が40℃、圧力が80Kg/cm2
超臨界状態の二酸化炭素を10ml/minの流量で3
0分間供給し分画した。気−液分離塔内で二酸化炭素と
溶出された精油を分離し、プソラレン類を含有しない精
油約0.9gを得た。
According to a preferred embodiment of the method of the present invention, for example, about 1 g of the natural essential oil as exemplified above is injected into a column filled with Amberlite XAD-7 by an injector, and the temperature is 40 ° C. and the pressure is 40 ° C. 80 kg / cm 2 of supercritical carbon dioxide at a flow rate of 10 ml / min.
It was fed for 0 minutes and fractionated. The carbon dioxide and the eluted essential oil were separated in the gas-liquid separation column to obtain about 0.9 g of a psoralen-free essential oil.

【0022】本発明により得られた精油は、ガスクロマ
トグラフ分析により、プソラレン類を実質的に含有して
いないことを確認した。また、得られた精油は、元の天
然精油の香気成分バランスを有していた。
The essential oil obtained according to the present invention was confirmed by gas chromatography analysis to be substantially free of psoralens. Further, the obtained essential oil had a fragrance component balance of the original natural essential oil.

【0023】[0023]

【実施例】以下、実施例により、本発明方法の数態様に
ついて更に詳しく説明する。
The following examples further illustrate several aspects of the method of the present invention.

【0024】実施例1 日本分光Super−201型超臨界二酸化炭素抽出ク
ロマト装置を用いた。10ml容積の抽出カラムに多孔
性吸着樹脂アンバーライトXAD−7(Rohm&Ha
as社製)3.3gを充填し、温度40℃、圧力80k
g/cm2の超臨界状態の二酸化炭素を10ml/分で
供給しているところにベルガモット油(Ci Pro.Straczi
社製)856mgを注入し、30分間抽出した。気−液
分離塔内から、ベルガプテン(プソラレン類の一種)を
含有しない精油738mg(収率86%)を得た。ガス
クロマトグラフ分析により、プソラレン類は1ppm以
下であり、実質的にプソラレン類を含有していないこと
を確認した。
Example 1 A JASCO Super-201 type supercritical carbon dioxide extraction chromatograph was used. A porous adsorption resin Amberlite XAD-7 (Rohm & Ha) was applied to a 10 ml extraction column.
(manufactured by As Corporation), 3.3 g, temperature 40 ° C, pressure 80k
g / cm 2 of supercritical carbon dioxide at a rate of 10 ml / min is supplied with bergamot oil (Ci Pro. Straczi
856 mg) and extracted for 30 minutes. From the gas-liquid separation column, 738 mg (86% yield) of an essential oil not containing bergapten (a type of psoralen) was obtained. Gas chromatographic analysis confirmed that psoralens were 1 ppm or less, and that psoralens were not substantially contained.

【0025】実施例2〜4 実施例1と同様にして、多孔性吸着樹脂をHP10に代
えてベルガモット油を、また、ベルガモット油に代えて
レモン油を用いてプソラレン類を含有しない精油を得
た。それらを表1に示した。
Examples 2 to 4 In the same manner as in Example 1, an essential oil containing no psoralens was obtained using bergamot oil instead of HP10 as the porous adsorption resin and lemon oil instead of bergamot oil. . They are shown in Table 1.

【0026】[0026]

【表1】 実施例 試料 吸着樹脂 分離条件 抽出時間 収率 1 ヘ゛ルカ゛モツト XAD-7 40℃ 80kg/cm210ml/min 30分間 86% 2 ヘ゛ルカ゛モツト HP10 40℃ 80kg/cm210ml/min 30分間 81% 3 レモン XAD-7 40℃ 80kg/cm210ml/min 30分間 90% 4 レモン HP10 40℃ 80kg/cm210ml/min 30分間 87%[Table 1] Example Sample Adsorption resin Separation conditions Extraction time Yield 1 Balka mot XAD-7 40 ℃ 80kg / cm 2 10ml / min 30min 86% 2 Balka mot HP10 40 ℃ 80kg / cm 2 10ml / min 30min 81% 3 Lemon XAD-7 40 ° C 80kg / cm 2 10ml / min 30 minutes 90% 4 Lemon HP10 40 ° C 80kg / cm 2 10ml / min 30 minutes 87%

【0027】比較例1〜4 多孔性吸着樹脂の代わりにシリカゲルを用いた他は実施
例1と同様にして、ベルガモット油及びレモン油を用い
て、プソラレン類を除去した精油を得た。それらを表2
に示した。
Comparative Examples 1-4 Essential oils from which psoralens were removed were obtained using bergamot oil and lemon oil in the same manner as in Example 1 except that silica gel was used instead of the porous adsorption resin. Table 2
It was shown to.

【0028】[0028]

【表2】 比較例 試料 吸着樹脂 分離条件 抽出時間 収率 1 ヘ゛ルカ゛モツト シリカケ゛ル 40℃ 80kg/cm210ml/min 30分間 64% 2 ヘ゛ルカ゛モツト シリカケ゛ル 40℃ 100kg/cm210ml/min 30分間 76% 3 レモン シリカケ゛ル 40℃ 80kg/cm210ml/min 30分間 71% 4 レモン シリカケ゛ル 40℃ 100kg/cm210ml/min 30分間 82%TABLE 2 Comparative Sample adsorption resin separation condition extraction time yield 1 Berga Motsuto silica gel 40 ℃ 80kg / cm 2 10ml / min 30 min 64% 2 Berga Motsuto silica gel 40 ℃ 100kg / cm 2 10ml / min 30 minutes 76% 3 Lemon silica gel 40% 80 kg / cm 2 10 ml / min 30 minutes 71% 4 Lemon silica gel 40 ° C 100 kg / cm 2 10 ml / min 30 minutes 82%

【0029】香気判定結果 実施例1〜4及び比較例1〜4で得られた精油につい
て、よく訓練された5名のパネラーにより官能評価によ
る香気判定を行った。その結果を表3に示した。いずれ
の場合も、本発明により得られた精油は元の精油の香気
バランスを保持していて比較例より好ましいと判定され
た。
Aroma determination results The essential oils obtained in Examples 1 to 4 and Comparative Examples 1 to 4 were subjected to sensory evaluation by sensory evaluation by five well-trained panelists. Table 3 shows the results. In each case, the essential oil obtained according to the present invention maintained the aroma balance of the original essential oil and was judged to be preferable to the comparative examples.

【0030】[0030]

【表3】 香気判定結果 香気評価 香気判定 実施例1 ナチュラル感があり匂いがきれい。 5 実施例2 ナチュラル感があり匂いがきれい。 5 比較例1 やや甘さ香気が弱い。 4 比較例2 ややテルペン感が強い。 3 実施例3 ナチュラル感がありフレッシュ感も保持。 5 実施例4 実施例3と大差なし。 5 比較例3 フレッシュ感が弱い。 4 比較例4 ややテルペン感が強い。 3[Table 3] Odor judgment result Odor evaluation Odor judgment Example 1 Natural odor and beautiful odor. 5 Example 2 Natural feeling and smell are beautiful. 5 Comparative Example 1 Slightly sweet aroma was weak. 4 Comparative Example 2 Slightly strong terpene feeling. 3 Example 3 A natural feeling and a fresh feeling are maintained. 5 Example 4 No great difference from Example 3. 5 Comparative Example 3 Fresh feeling is weak. 4 Comparative Example 4 Somewhat strong terpene feeling. 3

【0031】香気評価及び香気判定は、プソラレン類除
去処理前のベルガモット油及びレモン油を標準にして行
った。香気判定基準は下記の通り。 5・・・標準サンプルと大差なし 4・・・標準サンプルとやや差あり 3・・・標準サンプルと差あり 2・・・標準サンプルとかなり差あり 1・・・標準サンプルと大差あり
The aroma evaluation and the aroma determination were performed using bergamot oil and lemon oil as standard before the psoralens removal treatment. The odor criteria are as follows. 5: not much different from standard sample 4 ... slightly different from standard sample 3 ... different from standard sample 2 ... significantly different from standard sample 1 ... significantly different from standard sample

【0032】[0032]

【発明の効果】本発明によれば、皮膚に有害作用を与え
る原因となるプソラレン類を含有する天然精油から該原
因物質を、天然精油の香気、その成分バランス、収量な
どに悪影響を与えることなしに、工業的に容易な手段で
有利に除去でき、しかして品質の優れた実質的にプソラ
レン類を含有しない天然精油を製造できる。
Industrial Applicability According to the present invention, a natural essential oil containing psoralens, which causes a harmful effect on the skin, can remove the causative substance from the natural essential oil without affecting the aroma of the natural essential oil, its component balance, yield, etc. In addition, natural essential oils which can be advantageously removed by industrially easy means and which are substantially free of psoralens of high quality can be produced.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明で使用する超臨界二酸化炭素抽出カラム
クロマト装置の概略構成図である。
FIG. 1 is a schematic configuration diagram of a supercritical carbon dioxide extraction column chromatograph used in the present invention.

【符号の説明】[Explanation of symbols]

1 ボンベ 2 予熱カラム 3 インジエクター 4 六方バルブ 5 分離カラム 6 恒温槽 7 検出器 8 トラップ 9 安全弁 v1 ストップバルブ v2 流量調節弁 Reference Signs List 1 cylinder 2 preheating column 3 injector 4 hexagonal valve 5 separation column 6 constant temperature bath 7 detector 8 trap 9 safety valve v1 stop valve v2 flow control valve

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 プソラレン類を含有する天然精油を、亜
臨界又は超臨界状態の二酸化炭素を流体として、多孔性
重合樹脂を充填した超臨界二酸化炭素抽出カラムクロマ
ト装置を用い、該天然精油中のプソラレン類を分画せし
めることを特徴とする、プソラレン類を含有しない天然
精油の製造法。
1. A method for producing a natural essential oil containing psoralens using a subcritical or supercritical carbon dioxide as a fluid, using a supercritical carbon dioxide extraction column chromatograph packed with a porous polymerized resin. A method for producing a natural essential oil containing no psoralens, comprising fractionating psoralens.
JP13917697A 1997-05-15 1997-05-15 Preparation of natural essential oil which does not contain psoralen compound Pending JPH10316991A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13917697A JPH10316991A (en) 1997-05-15 1997-05-15 Preparation of natural essential oil which does not contain psoralen compound

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13917697A JPH10316991A (en) 1997-05-15 1997-05-15 Preparation of natural essential oil which does not contain psoralen compound

Publications (1)

Publication Number Publication Date
JPH10316991A true JPH10316991A (en) 1998-12-02

Family

ID=15239350

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13917697A Pending JPH10316991A (en) 1997-05-15 1997-05-15 Preparation of natural essential oil which does not contain psoralen compound

Country Status (1)

Country Link
JP (1) JPH10316991A (en)

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* Cited by examiner, † Cited by third party
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JP2007163198A (en) * 2005-12-12 2007-06-28 Soda Aromatic Co Ltd Continuous evaluation method of volatile component and dispensing device
JP2011067179A (en) * 2009-09-28 2011-04-07 Toyo Institute Of Food Technology Method for producing fig decreased in furocoumarin content
CN102533446A (en) * 2012-01-10 2012-07-04 佰香汇生物科技(厦门)有限公司 New method for removing furocoumarins from citrus essential oil
CN105132181A (en) * 2015-08-10 2015-12-09 上海震樨机电科技发展有限公司 Process for extracting paeonia suffruticosa essential oil from paeonia suffruticosa fresh flower
CN106811300A (en) * 2015-12-01 2017-06-09 盐城润野生物科技有限公司 A kind of supercritical CO2The method for extracting Spartina alterniflora's essential oil
CN115141085A (en) * 2022-06-02 2022-10-04 上海天矩实业有限公司 Extraction and purification method of bakuchiol

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007163198A (en) * 2005-12-12 2007-06-28 Soda Aromatic Co Ltd Continuous evaluation method of volatile component and dispensing device
JP4609943B2 (en) * 2005-12-12 2011-01-12 曽田香料株式会社 Method and apparatus for continuous evaluation of volatile components
JP2011067179A (en) * 2009-09-28 2011-04-07 Toyo Institute Of Food Technology Method for producing fig decreased in furocoumarin content
CN102533446A (en) * 2012-01-10 2012-07-04 佰香汇生物科技(厦门)有限公司 New method for removing furocoumarins from citrus essential oil
CN105132181A (en) * 2015-08-10 2015-12-09 上海震樨机电科技发展有限公司 Process for extracting paeonia suffruticosa essential oil from paeonia suffruticosa fresh flower
CN106811300A (en) * 2015-12-01 2017-06-09 盐城润野生物科技有限公司 A kind of supercritical CO2The method for extracting Spartina alterniflora's essential oil
CN115141085A (en) * 2022-06-02 2022-10-04 上海天矩实业有限公司 Extraction and purification method of bakuchiol
CN115141085B (en) * 2022-06-02 2024-03-19 上海天矩实业有限公司 Method for extracting and purifying bakuchiol

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