[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

JPH06116171A - Method for purifying natural squalene - Google Patents

Method for purifying natural squalene

Info

Publication number
JPH06116171A
JPH06116171A JP26758692A JP26758692A JPH06116171A JP H06116171 A JPH06116171 A JP H06116171A JP 26758692 A JP26758692 A JP 26758692A JP 26758692 A JP26758692 A JP 26758692A JP H06116171 A JPH06116171 A JP H06116171A
Authority
JP
Japan
Prior art keywords
squalene
purity
acetone
purified
natural
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
JP26758692A
Other languages
Japanese (ja)
Inventor
Sadaya Kitazawa
貞哉 北沢
Ikuko Noguchi
生子 野口
Toshiyuki Sakakibara
敏之 榊原
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.)
Nippon Fine Chemical Co Ltd
Original Assignee
Nippon Fine Chemical 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 Nippon Fine Chemical Co Ltd filed Critical Nippon Fine Chemical Co Ltd
Priority to JP26758692A priority Critical patent/JPH06116171A/en
Publication of JPH06116171A publication Critical patent/JPH06116171A/en
Pending legal-status Critical Current

Links

Landscapes

  • Cosmetics (AREA)
  • Acyclic And Carbocyclic Compounds In Medicinal Compositions (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

PURPOSE:To purify a natural squalene useful for medicines, cosmetics, etc., having high purity, high quality and excellent safety free from color, smell and tastes by crystallizing a squalene having a given or higher purity under a specific condition. CONSTITUTION:Squalene having 98% or higher purity purified by distillation is dissolved in acetone 5-10 times as much as that of the squalene, cooled to-10 to-94 deg.C and crystallized and purified to give a natural squalene having 99.5% or higher purity.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、食品、化粧品及び医薬
品の分野で十分に使用できる、色、臭い及び味のない高
度に精製された高品質かつ安全性の高い天然スクワレン
を提供する方法に関する。
FIELD OF THE INVENTION The present invention relates to a method for providing highly purified, high-quality and safe natural squalene free from color, odor and taste, which can be sufficiently used in the fields of food, cosmetics and pharmaceuticals. .

【0002】[0002]

【従来技術及びその問題点】天然スクワレンは、6個の
イソプレン残基からなる炭素数30の分子鎖状構造を持
つ不飽和天然炭化水素化合物であり、魚介類、特に深海
産の鮫の肝臓に多く含まれ、古くから皮膚の外用薬や健
康食品などに幅広く用いられ、また、化粧品や医薬の添
加剤としての応用も期待されていた。さらに、水素添加
によりスクワランとした後、化粧品および潤滑剤として
も使用されている。スクワレン本来の生理作用として
は、細胞内に浸透して細胞の働きを賦活する作用が挙げ
られ、化粧品や外用薬として皮膚に適用することによ
り、皮膚の老化を防ぐことや、内服した場合に胃潰瘍や
肝疾患に有効であることが見出されてきており、これに
伴い、天然スクワレンの需要が年々高まってきている。
2. Description of the Related Art Natural squalene is an unsaturated natural hydrocarbon compound having a molecular chain structure of 30 carbon atoms consisting of 6 isoprene residues, and is used in fish and shellfish, especially in the deep sea shark liver. Since it is contained in large amounts, it has been widely used as an external medicine for skin and health food since ancient times, and it has been expected to be applied as an additive for cosmetics and medicines. Further, it has been used as a cosmetic and a lubricant after being made into squalane by hydrogenation. The original physiological effects of squalene include the effect of penetrating into cells and activating the function of cells, and by applying it to the skin as a cosmetic or external medicine, it prevents skin aging, and gastric ulcers when taken internally. It has been found to be effective for liver diseases and liver diseases, and along with this, the demand for natural squalene is increasing year by year.

【0003】従来、このように有用性の高い天然スクワ
レンは、鮫の肝油等のスクワレンを多量に含むオイルを
ケン化分解して粗スクワレンを得、この粗スクワレンを
減圧蒸留して製品化していた。
Conventionally, such highly useful natural squalene has been commercialized by saponifying and decomposing crude squalene with oil containing a large amount of squalene such as shark liver oil. .

【0004】しかし、減圧蒸留のみによる従来法では不
純物や戻り臭を完全に取り除くのは不可能であり、着色
や臭いが残存するため、例えば化粧品などの美感が問題
とされる用途に用いるのに十分な品質のものは得られて
いなかった。また、蒸留のみでは、皮膚などに対し悪影
響を及ぼすスクワレン酸化物を十分に低濃度まで除去す
ることができず、安全性の点でも問題があった。
However, it is impossible to completely remove impurities and returning odor by the conventional method using only vacuum distillation, and coloring and odor remain, so that it is used in applications such as cosmetics where aesthetics are a problem. It was not of sufficient quality. Further, squalene oxide, which adversely affects the skin and the like, cannot be removed to a sufficiently low concentration only by distillation, and there is a problem in terms of safety.

【0005】天然スクワレンの他の精製方法としては、
粗スクワレンを1〜2倍量のアセトンで再結晶を3回繰
り返した後、シリカゲルカラムを通してスクワレンの標
準サンプルを得る方法が報告されている(K. J. Sax 及
び F. H. Stross., ANAL. CHEM., 29, 1700 (1957)参
照)。しかしながら、本発明者がこの方法を追試してみ
ると、1%程度の不純物を除去することができず、化粧
品等の用途として好適なスクワレンは得られないことが
判明した。すなわち、シリカゲルカラムを通すことによ
り着色や臭い成分の量は軽減ないし除去できるが、スク
ワレンは反応性の高い不飽和結合を多数有しており、シ
リカゲルカラムによる精製中に過酸化された分解物が新
たに生じるため、この分解物を除去することができず、
99%以上の高純度のスクワレンは得られなかった。ま
た、シリカゲルカラムによる精製は、工業的用途に適さ
ず、回収率が低いという問題点もある。
Other methods for purifying natural squalene include:
A method for obtaining a standard sample of squalene through a silica gel column after repeating recrystallization of crude squalene with 1 to 2 times the amount of acetone three times has been reported (KJ Sax and FH Stross., ANAL. CHEM., 29, 1700 (1957)). However, when the present inventor tried this method additionally, it was found that impurities of about 1% could not be removed, and squalene suitable for use in cosmetics and the like could not be obtained. That is, the amount of coloring and odorous components can be reduced or removed by passing through a silica gel column, but squalene has a large number of highly reactive unsaturated bonds, and decomposition products that are peroxidized during purification by a silica gel column are Since it is newly generated, this decomposition product cannot be removed,
High-purity squalene of 99% or more could not be obtained. Further, the purification by silica gel column is not suitable for industrial use, and there is a problem that the recovery rate is low.

【0006】従来、減圧蒸留のみにより精製されていた
のも、それ以上の精製が困難であったからである。この
様に、天然スクワレンを高度に精製するのは容易ではな
く、現在または将来にかけての安価なスクワレンの大量
供給の要請を満たすために、簡易且つ高純度にスクワレ
ンを精製する方法の開発が大きな課題となっている。
Conventionally, purification was performed only by vacuum distillation, because further purification was difficult. Thus, it is not easy to highly purify natural squalene, and in order to meet the demand for large-scale supply of inexpensive squalene at present or in the future, development of a method for simply and highly purifying squalene is a major issue. Has become.

【0007】[0007]

【発明が解決しようとする課題】本発明は、無味無臭無
色且つ過酸化物を有しない高純度かつ安全性の高い天然
スクワレンを提供することを目的とする。
DISCLOSURE OF THE INVENTION It is an object of the present invention to provide natural squalene having high purity and high safety which is tasteless, odorless, colorless and has no peroxide.

【0008】[0008]

【課題を解決するための手段】本発明者は、上記課題を
解決するため鋭意検討を重ねた結果、減圧蒸留により粗
精製したスクワレンを特定の量のアセトン中低温で再結
晶することにより、高純度のスクワレンが容易に得られ
ることを見出した。
Means for Solving the Problems The inventors of the present invention have conducted extensive studies to solve the above problems, and as a result, recrystallized squalene roughly purified by vacuum distillation at a low temperature in a specific amount of acetone to obtain a high yield. It has been found that pure squalene is easily obtained.

【0009】即ち、本発明は、蒸留精製により純度98
%以上としたスクワレンを、該スクワレンの5〜10倍
量のアセトンに溶解し、−10℃〜−94℃に冷却して
結晶化することを特徴とする純度99.5%以上の天然
スクワレンの精製方法を提供するものである。
That is, the present invention has a purity of 98 by distillation purification.
% Of squalene is dissolved in 5 to 10 times the amount of acetone of the squalene and cooled to −10 ° C. to −94 ° C. for crystallization to crystallize 99.5% or more of natural squalene. A purification method is provided.

【0010】なお、スクワレンの純度は、キャピラリー
カラムを用いてガスクロマトグラフィーにより求めた純
度である。その測定条件を以下に示す。
The purity of squalene is the purity determined by gas chromatography using a capillary column. The measurement conditions are shown below.

【0011】* カラム:ウルトラ−I(ヒューレット
パッカード社製) 25m × 0.2mm i.d. * 検出器:FID検出器 * キャリヤーガス:ヘリウム * 流量(入口圧):0.8kg/cm2 * カラム温度:280℃(恒温分析) * インジェクション温度:300℃ 本発明で精製する天然スクワレンの原料としては、鮫の
肝油、オリーブ油、イースト脂肪その他の動植物油など
が挙げられ、特に深海産の鮫の肝油がスクワレン含量が
著しく高いため好ましい。
* Column: Ultra-I (manufactured by Hewlett-Packard Co.) 25 m × 0.2 mm i. d. * Detector: FID detector * Carrier gas: Helium * Flow rate (inlet pressure): 0.8 kg / cm 2 * Column temperature: 280 ° C (isothermal analysis) * Injection temperature: 300 ° C Raw material of natural squalene purified by the present invention Examples thereof include shark liver oil, olive oil, yeast fat and other animal and vegetable oils. Particularly, deep-sea shark liver oil is preferable because it has a significantly high squalene content.

【0012】該原料を、定法に従い減圧蒸留することに
より純度98%以上の粗スクワレンを得ることができ
る。再結晶に供する粗スクワレンの純度が98%を下回
ると、後の再結晶により化粧品等の用途に用いるのに十
分な純度のスクワレンを得るために再結晶を繰り返す必
要があり、回収率が低下するため好ましくない。
Crude squalene having a purity of 98% or more can be obtained by subjecting the raw material to vacuum distillation according to a conventional method. If the purity of the crude squalene used for recrystallization is less than 98%, it is necessary to repeat the recrystallization in order to obtain squalene having a sufficient purity for use in cosmetics and the like by the subsequent recrystallization, and the recovery rate decreases. Therefore, it is not preferable.

【0013】得られた粗スクワレンは、アセトンから再
結晶して精製する。使用するアセトンの量は、粗スクワ
レンの5〜10倍量、即ち、粗スクワレン1重量部当た
り5〜10重量部である。アセトンの量が5倍量未満に
なると、結晶化したスクワレン中の不純物が増加するた
め好ましくない。なお、5倍量未満のアセトンを用いて
再結晶を繰り返したとしても、不純物の除去は困難であ
り、また回収率も下がることになる。また、アセトンの
量が10倍量を超えると、スクワレンの回収率が低下す
るため好ましくない。粗スクワレンは、上記量のアセト
ン中に室温で溶解し、必要により濾過した後冷却して2
〜6時間程度放置する。冷却温度は、−10℃〜−94
℃、好ましくは−30〜−70℃程度、より好ましくは
−30〜−50℃程度である。冷却温度が−10℃以上
になると結晶化に長時間を要するようになり、また回収
率も低下するため好ましくない。冷却温度が−94℃よ
り低下すると、再結晶溶媒のアセトンが凝固する可能性
があり好ましくない。なお、粗スクワレンの着色が著し
いときは、吸着剤等で脱色を行った後、再結晶しても良
い。析出した結晶を濾取し、室温に戻して溶かした後、
真空下で乾燥することにより、99.5%以上の純度の
精製スクワレンを得ることができる。その回収率は、蒸
留後の上記粗スクワレンを基準として80%以上であ
る。なお、再結晶に使用するアセトンは、脱酸素したア
セトンを用いるのが好ましい。脱酸素したアセトンは、
例えば、アセトン中への不活性ガスの吹き込み、不活性
ガス雰囲気化でのアセトンの蒸留精製、超音波照射によ
る脱気、気体膜透過による分離などが挙げられる。不活
性ガスとしては、窒素、アルゴン、ヘリウム、炭酸ガス
などが例示される。また、再結晶は、酸化物の生成を抑
制するため不活性ガス雰囲気下で行うのが好ましい。
The crude squalene obtained is purified by recrystallization from acetone. The amount of acetone used is 5 to 10 times the amount of crude squalene, that is, 5 to 10 parts by weight per 1 part by weight of crude squalene. If the amount of acetone is less than 5 times, the amount of impurities in the crystallized squalene increases, which is not preferable. Even if recrystallization is repeated using less than 5 times the amount of acetone, it is difficult to remove impurities, and the recovery rate is also lowered. Further, if the amount of acetone exceeds 10 times, the recovery rate of squalene decreases, which is not preferable. The crude squalene is dissolved in the above-mentioned amount of acetone at room temperature, filtered if necessary, and then cooled to 2
Leave for about 6 hours. The cooling temperature is -10 ° C to -94.
C, preferably about -30 to -70 ° C, more preferably about -30 to -50 ° C. If the cooling temperature is -10 ° C or higher, it takes a long time for crystallization and the recovery rate is lowered, which is not preferable. If the cooling temperature is lower than -94 ° C, acetone as a recrystallization solvent may be solidified, which is not preferable. When the crude squalene is markedly colored, it may be recrystallized after being decolorized with an adsorbent or the like. The precipitated crystals were collected by filtration, returned to room temperature and dissolved,
By drying under vacuum, purified squalene having a purity of 99.5% or more can be obtained. The recovery rate is 80% or more based on the crude squalene after distillation. As the acetone used for recrystallization, it is preferable to use deoxidized acetone. Deoxygenated acetone is
Examples thereof include blowing an inert gas into acetone, distilling and purifying acetone in an inert gas atmosphere, degassing by ultrasonic irradiation, and separation by gas membrane permeation. Examples of the inert gas include nitrogen, argon, helium, carbon dioxide gas and the like. In addition, recrystallization is preferably performed in an inert gas atmosphere in order to suppress oxide formation.

【0014】[0014]

【発明の効果】本発明によれば、再結晶溶媒の特定の量
及び冷却温度を選択することにより、従来高度に精製す
ることが困難であったスクワレンを、非常に容易に9
9.5%以上の純度まで精製できるようになった。しか
も、その回収率も非常に高い。
According to the present invention, by selecting a specific amount of a recrystallization solvent and a cooling temperature, squalene, which has hitherto been difficult to highly purify, can be very easily prepared.
It became possible to purify to a purity of 9.5% or more. Moreover, its recovery rate is also very high.

【0015】また、得られた精製スクワレンは、無味無
色無臭かつ酸化物をほとんど含まないため、品質及び安
全性の観点から使用が制限されていた医薬品及び化粧品
の基剤及び食品として、広範な応用が期待できる。
The purified squalene obtained is tasteless, colorless and odorless and contains almost no oxides, and therefore has a wide range of applications as bases and foods for pharmaceuticals and cosmetics, the use of which has been limited in terms of quality and safety. Can be expected.

【0016】[0016]

【実施例】以下、本発明を実施例及び比較例を用いてよ
り詳しく説明する。
EXAMPLES The present invention will be described in more detail below with reference to examples and comparative examples.

【0017】実施例1 鮫肝油を水酸化ナトリウムによりケン化分解した後、不
ケン化物について減圧蒸留を3回繰り返し、沸点252
〜254℃/5mmHgの留分として、純度99.0%
の粗スクワレンを得た。この粗スクワレン100g不活
性ガス雰囲気下に、脱酸素したアセトン700gに室温
で溶解し、約−50℃に冷却して3時間放置して結晶化
させた。得られた結晶を濾過して集め、室温に戻して結
晶を溶かし、アセトンをキャピラリーを用いて僅かに窒
素を流しながら減圧留去して純粋な天然スクワレン95
gを得た。得られた精製物のキャピラリーカラムでのガ
スクロマトグラフィーによる純度は、99.9%であっ
た。なお、純度を示すガスクロマトグラフィーのチャー
トを図1に示す。また、得られたスクワレンは、色、味
及び臭いはなく、基準油脂分析試験法2.4.12−7
1により求めた過酸化物価は0.2であった。
Example 1 Shark liver oil was saponified and decomposed with sodium hydroxide, and then the unsaponifiable matter was distilled under reduced pressure three times to give a boiling point of 252.
As a fraction of ˜254 ° C./5 mmHg, purity 99.0%
Of crude squalene was obtained. 100 g of this crude squalene was dissolved in 700 g of deoxidized acetone at room temperature in an inert gas atmosphere, cooled to about -50 ° C, and allowed to stand for 3 hours for crystallization. The obtained crystals were collected by filtration, returned to room temperature to dissolve the crystals, and acetone was distilled off under reduced pressure while slightly flowing nitrogen using a capillary to obtain pure natural squalene 95
g was obtained. The purity of the obtained purified product by gas chromatography using a capillary column was 99.9%. A gas chromatography chart showing the purity is shown in FIG. In addition, the obtained squalene has no color, taste and odor, and the standard oil and fat analysis test method 2.4.12-7
The peroxide value determined by 1 was 0.2.

【0018】比較例1 鮫肝油を水酸化ナトリウムによりケン化分解した後、不
ケン化物について減圧蒸留を2回繰り返し、沸点250
〜260℃/5mmHgの留分として、純度95.0%
の粗スクワレンを得た。得られた粗スクワレン100g
を、アセトン700gを用いて実施例1と同様にして再
結晶を行い、精製スクワレン80gを得た。得られた精
製スクワレンのガスクロマトグラフィーによる純度は、
98.0%で、色及び味はないが、わずかに臭いが残っ
ていた。また、このスクワレンの過酸化物価は、0.2
であった。
Comparative Example 1 Shark liver oil was saponified and decomposed with sodium hydroxide, and then the unsaponifiable matter was distilled twice under reduced pressure to give a boiling point of 250.
As a fraction of ~ 260 ° C / 5mmHg, purity 95.0%
Of crude squalene was obtained. 100 g of crude squalene obtained
Was recrystallized from 700 g of acetone in the same manner as in Example 1 to obtain 80 g of purified squalene. The purity of the obtained purified squalene by gas chromatography is
At 98.0%, there was no color or taste, but a slight odor remained. The peroxide value of this squalene is 0.2.
Met.

【0019】比較例2 実施例1で用いた純度99.0%のスクワレン100g
を、アセトン140gに溶解して実施例1と同様にして
再結晶を3回繰り返し、精製スクワレン60gを得た。
得られた精製スクワレンは、色、味及び臭いはなく、そ
のガスクロマトグラフィーによる純度は99.5%で、
その過酸化物価は、0.2であった。
Comparative Example 2 100 g of squalene having a purity of 99.0% used in Example 1
Was dissolved in 140 g of acetone and recrystallized three times in the same manner as in Example 1 to obtain 60 g of purified squalene.
The purified squalene obtained has no color, taste or odor, its gas chromatographic purity is 99.5%,
Its peroxide value was 0.2.

【0020】比較例3 実施例1で用いた純度99.0%のスクワレン100g
を、アセトン1500gに溶解した他は実施例1と同様
にして再結晶を行い、精製スクワレン60gを得た。得
られた精製スクワレンは、色、味及び臭いはなく、その
ガスクロマトグラフィーによる純度は99.5%で、そ
の過酸化物価は、0.2であった。
Comparative Example 3 100 g of squalene having a purity of 99.0% used in Example 1
Was dissolved in 1500 g of acetone and recrystallized in the same manner as in Example 1 to obtain 60 g of purified squalene. The purified squalene obtained had no color, taste or odor, its gas chromatographic purity was 99.5%, and its peroxide value was 0.2.

【0021】比較例4 実施例1で用いた純度99.0%のスクワレン100g
を、アセトン700gに溶解し、−5℃に冷却したが、
結晶化しなかった。
Comparative Example 4 100 g of squalene having a purity of 99.0% used in Example 1
Was dissolved in 700 g of acetone and cooled to -5 ° C.
It did not crystallize.

【0022】比較例5 実施例1で用いた純度99.0%のスクワレン100g
を、シリカゲルカラムを通して精製し(展開溶媒:ヘキ
サン)、スクワレン84gを回収した。得られた精製ス
クワレンのガスクロマトグラフィーによる純度は99.
0%で、着色・着臭があり、味も悪く、その過酸化物価
は、2.4であった。
Comparative Example 5 100 g of squalene having a purity of 99.0% used in Example 1
Was purified by passing through a silica gel column (developing solvent: hexane), and 84 g of squalene was recovered. The purity of the obtained purified squalene by gas chromatography is 99.
At 0%, there was coloring and odor, the taste was bad, and the peroxide value was 2.4.

【0023】実施例1及び比較例1〜5の結果をまとめ
て、以下の表1に示す。
The results of Example 1 and Comparative Examples 1 to 5 are summarized in Table 1 below.

【0024】[0024]

【表1】 [Table 1]

【0025】なお、表1中、色はAPHA法により求め
た。また、味および臭いは5人のパネラーにより評価し
た。味および臭いの評価は、以下のようにして行った。
The colors in Table 1 were determined by the APHA method. The taste and smell were evaluated by 5 panelists. The taste and odor were evaluated as follows.

【0026】* 味:再結晶前後のサンプルを各々5〜
20mlを口の中に含むかまたは飲み込んだ場合にどの
ような味が感じられるかを比較した。
* Taste: 5 to 5 samples before and after recrystallization
The taste was felt when 20 ml was included in the mouth or swallowed.

【0027】* 臭い:再結晶前後のサンプル各々10
mlを20mlのサンプル瓶にいれてよく振り混ぜた
後、蓋を開けた直後の臭いを比較した。さらに、少量の
サンプルを手の甲に塗り、そのときに臭いがあるかどう
かを比較した、 表1の結果から、本発明の精製方法によれば、色、臭い
及び味のないスクワレンを容易に得ることができ、しか
もその回収率も高く、本発明の精製方法が極めて優れて
いることが明らかとなった。
* Odor: 10 samples each before and after recrystallization
After adding ml to a 20 ml sample bottle and shaking well, the odor immediately after opening the lid was compared. Furthermore, a small amount of sample was applied to the back of the hand, and whether or not there was odor at that time was compared. From the results in Table 1, according to the purification method of the present invention, squalene having no color, odor and taste can be easily obtained. It was revealed that the purification method of the present invention was extremely excellent because of its high recovery rate.

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

【図1】実施例1で得られた精製スクワレンのガスクロ
マトグラフのチャートである。
1 is a gas chromatograph chart of purified squalene obtained in Example 1. FIG.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 A61K 31/01 ADA 9283−4C ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification number Office reference number FI technical display location A61K 31/01 ADA 9283-4C

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】蒸留精製により純度98%以上としたスク
ワレンを、該スクワレンの5〜10倍量のアセトンに溶
解し、−10℃〜−94℃に冷却して結晶化することを
特徴とする純度99.5%以上の天然スクワレンの精製
方法。
1. A squalene having a purity of 98% or more obtained by distillation purification is dissolved in 5 to 10 times the amount of acetone of the squalene and cooled to -10 ° C. to -94 ° C. for crystallization. A method for purifying natural squalene having a purity of 99.5% or more.
JP26758692A 1992-10-06 1992-10-06 Method for purifying natural squalene Pending JPH06116171A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26758692A JPH06116171A (en) 1992-10-06 1992-10-06 Method for purifying natural squalene

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26758692A JPH06116171A (en) 1992-10-06 1992-10-06 Method for purifying natural squalene

Publications (1)

Publication Number Publication Date
JPH06116171A true JPH06116171A (en) 1994-04-26

Family

ID=17446824

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26758692A Pending JPH06116171A (en) 1992-10-06 1992-10-06 Method for purifying natural squalene

Country Status (1)

Country Link
JP (1) JPH06116171A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008102032A1 (en) * 2007-02-22 2008-08-28 Universidad De Cordoba Method for obtaining squalene
JP2008222686A (en) * 2007-03-16 2008-09-25 Rofutei:Kk Pharmaceutical and functional food imparting blood fluidity ameliorating activity
WO2011141819A1 (en) * 2010-05-12 2011-11-17 Novartis Ag Improved methods for preparing squalene
WO2012169443A1 (en) * 2011-06-06 2012-12-13 Jx日鉱日石エネルギー株式会社 Method for manufacturing refined vegetable squalene and refined vegetable squalene
US11236366B2 (en) 2008-08-28 2022-02-01 Novartis Ag Production of squalene from hyper-producing yeasts

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008102032A1 (en) * 2007-02-22 2008-08-28 Universidad De Cordoba Method for obtaining squalene
ES2304102A1 (en) * 2007-02-22 2008-09-01 Universidad De Cordoba Method for obtaining squalene
JP2008222686A (en) * 2007-03-16 2008-09-25 Rofutei:Kk Pharmaceutical and functional food imparting blood fluidity ameliorating activity
US11236366B2 (en) 2008-08-28 2022-02-01 Novartis Ag Production of squalene from hyper-producing yeasts
EP2569267B2 (en) 2010-05-12 2017-03-22 Novartis AG Improved methods for preparing squalene
CN102892734A (en) * 2010-05-12 2013-01-23 诺华有限公司 Improved methods for preparing squalene
EP2620423A1 (en) * 2010-05-12 2013-07-31 Novartis AG Improved methods for preparing squalene
AU2011251706B2 (en) * 2010-05-12 2015-10-22 Seqirus UK Limited Improved methods for preparing squalene
US9199897B2 (en) 2010-05-12 2015-12-01 Novartis Ag Methods for preparing squalene
CN105125488A (en) * 2010-05-12 2015-12-09 诺华股份有限公司 Improved methods for preparing squalene
EP2620423B1 (en) 2010-05-12 2016-07-20 Novartis AG Improved methods for preparing squalene
US9545440B2 (en) 2010-05-12 2017-01-17 Novartis Ag Methods for preparing squalene
US9867877B2 (en) 2010-05-12 2018-01-16 Novartis Ag Methods for preparing squalene
EP3489211A1 (en) * 2010-05-12 2019-05-29 Novartis AG Improved methods for preparing squalene
EP2620423B2 (en) 2010-05-12 2019-07-31 Novartis AG Improved methods for preparing squalene
WO2011141819A1 (en) * 2010-05-12 2011-11-17 Novartis Ag Improved methods for preparing squalene
WO2012169443A1 (en) * 2011-06-06 2012-12-13 Jx日鉱日石エネルギー株式会社 Method for manufacturing refined vegetable squalene and refined vegetable squalene

Similar Documents

Publication Publication Date Title
JP3241542B2 (en) Method for purifying (-)-n-isopulegol and citrus-based fragrance composition containing (-)-n-isopulegol obtained by the method
US6664405B2 (en) Method for isolating high-purified unsaturated fatty acids using crystallization
EP1065196B1 (en) Process of selectively separating and purifying eicosapentaenoic and docosahexaenoic acids or their esters
US7459587B2 (en) Process for purifying menthol
US5130449A (en) Isolation of stearidonic acid from fatty acid mixtures
AU2009290334B2 (en) Method for acquiring highly unsaturated fatty acid derivatives
JPH05294928A (en) Purification of phthalimidoperoxycaproric acid (pap)
CA2624376A1 (en) A process and an apparatus for producing episesamin-rich compositions
JPH06116171A (en) Method for purifying natural squalene
EP0912506A1 (en) PROCESS FOR THE RECOVERY OF CRYSTALLINE $g(b)-CAROTENE FROM A NATURAL SOURCE
JPS59133298A (en) Pepper mint oil stabilization
JP6234908B2 (en) Method for producing eicosapentaenoic acid and / or docosahexaenoic acid-containing composition
CA2628304C (en) Method of refining episesamin
JPH01207257A (en) Method for separating alpha-linolenic acid
JPH0790294A (en) Essential oil having high spilanthol content, production thereof and composition for oral cavity blended with essential oil having high spilanthol content
JPS61268677A (en) Methanol extraction of tocopherol
US20020025548A1 (en) Process for the recovery of crystalline beta-carotene from a natural source
JPS63190840A (en) Purification of solanesol
CN101503411B (en) Method for separating sesamine from gingelly oil
AU2002348729A1 (en) Process for crystallization of oryzanol from oryzanol enriched fraction derived from rice bran oil soap stock
JPS6339991A (en) Purification of animal oils and fats
JP2001335794A (en) Process for purifying docosahexaenoic acid or its derivative
JPS60243038A (en) Preparation of concentrated natural vitamin k
JPS60241908A (en) Manufacture of refined component from multicomponent raw material
CN116924930A (en) Purification method of cooling agent N-ethyl-2, 2-diisopropylbutanamide