JPH01284335A - Method and beads for separating and concentrating tocopherols - Google Patents

Method and beads for separating and concentrating tocopherols

Info

Publication number
JPH01284335A
JPH01284335A JP63112999A JP11299988A JPH01284335A JP H01284335 A JPH01284335 A JP H01284335A JP 63112999 A JP63112999 A JP 63112999A JP 11299988 A JP11299988 A JP 11299988A JP H01284335 A JPH01284335 A JP H01284335A
Authority
JP
Japan
Prior art keywords
tocopherols
beads
column
separating
concentrating
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.)
Granted
Application number
JP63112999A
Other languages
Japanese (ja)
Other versions
JP2757372B2 (en
Inventor
Toshiyuki Kobashi
小橋 利行
Ryosuke Nishida
良祐 西田
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.)
Japan Exlan Co Ltd
Original Assignee
Japan Exlan 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 Japan Exlan Co Ltd filed Critical Japan Exlan Co Ltd
Priority to JP63112999A priority Critical patent/JP2757372B2/en
Publication of JPH01284335A publication Critical patent/JPH01284335A/en
Application granted granted Critical
Publication of JP2757372B2 publication Critical patent/JP2757372B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

PURPOSE:To separate and concentrate high purity tocopherols with high work efficiency in a high yield by passing the deodorized distillate of fats and oils through a column for liq. chromatography packed with beads made of a polyvinyl compd.-based porous polymer and having a certain particle size or above and a certain water content or above in the form of gel. CONSTITUTION:Porous polymer beads having >=10mum particle size and, >=30% water content in the form of gel are produced with methacrylic acid, sodium p-styrenesulfonate, polyvinyl alcohol, ethylene glycol dimethacrylate, glycidyl methacrylate, epichlorohydrin, 2,2-azobis-(2,4-dimethylvaleronitrile) and formic acid. A column is packed with the beads and the deodorized distillate of soybean oil, etc., is poured into the column. Methanol as a developing medium is then passed through the column to separate and collect tocopherols by liq. chromatography. The resulting high purity tocopherols are used as vitamin E, an antioxidant, etc.

Description

【発明の詳細な説明】 (産業上の利用分If) 本発明は、トコフェロール類を分離a縮する際に用いる
ビーズ及び分離濃縮方法に関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application If) The present invention relates to beads used in separating and condensing tocopherols and a separation and concentration method.

(従来の技術) α、β、γおよびδ−トコフXロール等(以下、トコフ
ェロール類というンは、大豆油、菜樋油、尚来泊、サフ
ラワー油、米ぬか油、トウモロコシ油、ひまわシ油等の
脱臭工程で副生ずる脱臭留出物中に含有されているが、
該脱臭留出物中にはトコフェロール類の他に炭化水素類
、ステリン類、グリセリド、遊離脂肪酸等が共存してい
るために、ビタミンEとして医薬品に、また抗酸化剤と
して食品に直接使用し難い。
(Prior art) α, β, γ and δ-tocopherols, etc. (hereinafter referred to as tocopherols) It is contained in the deodorizing distillate that is produced as a by-product in the process of deodorizing oil, etc.
In addition to tocopherols, hydrocarbons, sterins, glycerides, free fatty acids, etc. coexist in this deodorized distillate, so it is difficult to use it directly in medicines as vitamin E or in foods as an antioxidant. .

従来から該脱臭留出物中のトコフェロ−/L/類をMM
濃硝するために、分子蒸留法、イオン交換樹脂処理等の
方法が用いられていたが、分子蒸留法では分備操作が困
難なうえに舖濃度の濃縮物を収率よく得ることは非常に
煙しく、またイオン交換樹脂処理法では樹脂がトコフェ
ロール類を特異的に吸着する方法であるため、分取に高
度な技術を要し、さらに樹脂の再生が必要で溶剤[侯を
行う場合に生ずる浴出架剤の除去処理等繁雑な工程を要
する欠点がおる。
Conventionally, tocopherols/L/s in the deodorized distillate have been treated with MM.
Methods such as molecular distillation and ion-exchange resin treatment have been used to concentrate nitrogen, but with molecular distillation, it is difficult to perform separate operations, and it is extremely difficult to obtain a concentrate with a certain concentration in a good yield. Furthermore, in the ion-exchange resin treatment method, the resin specifically adsorbs tocopherols, so advanced techniques are required for preparative separation, and the resin must be regenerated, resulting in problems with solvent [housing]. It has the disadvantage that it requires complicated steps such as removal of the bathing agent.

(@明が解決しようとする課題〉 本発明の目的は、トコフェロール類の分離、積層に適し
た分離濃縮用ビーズを提供することにある。
(Problems to be solved by @Mei) An object of the present invention is to provide beads for separation and concentration that are suitable for separating and stacking tocopherols.

本発明の池の目的は、該ビーズを用いて液体クロマトグ
ラフィーによシ、脱臭留出物からトコフェロール類を作
業性よく、さらに高純度、高収率で得る分順濃姻方法を
提供することにおる。
The object of the present invention is to provide a fractional concentration method for obtaining tocopherols from a deodorized distillate by liquid chromatography using the beads with good workability, high purity, and high yield. I'm in the middle of the day.

(課題を解決するための手段〉 上述した本発明の目的を達成し得るトコフェロール類の
分4濃縮用ビーズは、ポリビニル化合物を主成分とする
多孔性重合体からなり、該止合体の粒子径がio、a以
上で、かつゲル水分率が30%以上を有するものであう
、またトコフェロール類の分4−輪方法は、該ビーズを
充填した液体クロマトグツフィー用カラムに脱臭留出物
を注入した後展開溶媒を通面し、目的とするトコフェロ
ール類を分画、採取する手段によシ有利に行うことがで
きる。
(Means for Solving the Problems) Beads for concentrating tocopherols that can achieve the above-mentioned object of the present invention are made of a porous polymer containing a polyvinyl compound as a main component, and the particle size of the aggregate is io, a or more and a gel moisture content of 30% or more.The four-ring method for tocopherols is performed after injecting the deodorized distillate into a column for liquid chromatography filled with the beads. This can be advantageously carried out by passing a developing solvent through, fractionating and collecting the target tocopherols.

以下、本発明を詳述するが、本発明のビーズはポリビニ
ル化合物を60i、fit%以上、好ましくは30直量
%以上結合金有する多孔11重合体からなり、該恵合体
の粒子径は10μ以上、好ましくは20〜150μで、
かつビーズのゲル水分率が30%以上、好ましくは50
%以上であることが必要である。
The present invention will be described in detail below. The beads of the present invention are made of a porous 11 polymer having a polyvinyl compound of 60 i and a fit% or more, preferably 30% or more by weight, and the particle size of the composite is 10μ or more. , preferably 20 to 150μ,
and the gel moisture content of the beads is 30% or more, preferably 50%.
% or more.

ここで、ポリビニル化合物としては、エチレングリコー
ルジアクリレート、エチレングリコールジメタクリレー
ト、ジエチレンクリコールジアクリレート、ジエチレン
グリコールジメタクリレート、トリエチレングリコール
ジアクリレート、トリエチレングリコールジメタクリレ
ート、テトフエチレングリコールジアクリレート、テト
フエチレングリコールジメタクリレート、プロピレング
リコールジアクリレート、プロピレングリコールジメタ
クリレート、ジエチレンクリコールジアクリレート、ジ
プロピレングリコールジメタクリレート、トリメチロー
ルエタントリアクリレート、トリメチロールエタントリ
メタクリレート、トリメチロールプロパントリアクリレ
ート、トリメチロールプロパントリメタクリレート、テ
トヲメチロールメタンテトファクリレート、テトラメチ
ロールメタンテトフメタクリレート、ポリエチレングリ
コールジメタクリレート、ポリプロピレングリコールジ
メタクリレート、グリセリンジアクリレート、グリセリ
ンジメタクリレート、グリセリントリアクリレート、グ
リセリントリメタクリレート等の(メタンアクリル酸ポ
リオールエステル類;メタクリル酸ビニル、メタアクリ
ル酸アリル等の(メタンアクリル師ビニルエステル頬;
マレイン酸ジアリル、フマル帥ジアリlし、コハク酸ジ
アリル、炭酸ジアリル、シュウ酸ジアリル、アジ上ピン
醗ジアリル、セバシン酸ジアリル、酒石酸ジアリル、ジ
アリルアミン、トリアリルアミン、リン酸トリアリIし
、トリカルバリル酸トリアリル、アコニット酸トリアリ
〃、クエン舖トリアリル、  リアリルシアヌレート、
ト トリアリルイソシアヌレート等のポリアリル化合物M 
iジビニルベンゼン、トリビニルベンゼン等の芳香族ポ
リビニル化合物類などが挙げられる。
Here, the polyvinyl compounds include ethylene glycol diacrylate, ethylene glycol dimethacrylate, diethylene glycol diacrylate, diethylene glycol dimethacrylate, triethylene glycol diacrylate, triethylene glycol dimethacrylate, tetofethylene glycol diacrylate, and tetofethylene glycol diacrylate. Methacrylate, propylene glycol diacrylate, propylene glycol dimethacrylate, diethylene glycol diacrylate, dipropylene glycol dimethacrylate, trimethylolethane triacrylate, trimethylolethane trimethacrylate, trimethylolpropane triacrylate, trimethylolpropane trimethacrylate, tetramethylol (Methane acrylic acid polyol esters; vinyl methacrylate) such as methane tetophacrylate, tetramethylol methane tetoph methacrylate, polyethylene glycol dimethacrylate, polypropylene glycol dimethacrylate, glycerin diacrylate, glycerin dimethacrylate, glycerin triacrylate, and glycerin trimethacrylate. , allyl methacrylate (methane acrylic vinyl ester);
diallyl maleate, diallyl fumarate, diallyl succinate, diallyl carbonate, diallyl oxalate, diallyl diamide, diallyl sebacate, diallyl tartrate, diallylamine, triallylamine, triallyl phosphate, triallyl tricarballylate, Aconitic acid triallyl, citric acid triallyl, realyl cyanurate,
Polyallyl compound M such as triaryl isocyanurate
Examples include aromatic polyvinyl compounds such as divinylbenzene and trivinylbenzene.

なお、主成分でめる上記単量体と共に共電合し得る他の
単重体を適宜併用してもよく、このような他の単量体と
してはアクリル酸エチル、アクリル酸エチル、アクリル
酸エチル、ポリオキシアルキレンアクリレート等のアク
リル醗エステyvm及びメタクリル酸メチル、メタクリ
ル酸エチル、メタクリル酸グチル、ポリオキシアルキレ
ンメタクリレート等のメタクリル版エステル類並びに炭
素数3〜12のモノビニルカルボン飯のグリシジルエス
テル類及び炭素数8〜12のモノビニルアルコールのグ
リシジルエーテル類等を挙げることができる。
In addition, other monomers that can be coelectrified with the above-mentioned monomers which are the main components may be used in combination as appropriate. Examples of such other monomers include ethyl acrylate, ethyl acrylate, and ethyl acrylate. , acrylic esters such as polyoxyalkylene acrylate, methacrylic esters such as methyl methacrylate, ethyl methacrylate, butyl methacrylate, polyoxyalkylene methacrylate, and glycidyl esters of monovinyl carboxylic acid having 3 to 12 carbon atoms and carbon Examples include glycidyl ethers of monovinyl alcohol having numbers 8 to 12.

上記単量体は、公知の油溶性ラジカル重合開始剤を用い
、単量体との相容性には優れているが水との相容性はな
い有機溶剤である希釈剤の存在下で水系懸濁重合する等
周知の方法にょシ恵合を行うことができ、例えば特開昭
59−28104号公報及び特開昭60−165647
号公報記載の手段を採用することにより、多孔性重合体
からなるビーズを作製することができる。
The above monomers are produced in an aqueous system using a known oil-soluble radical polymerization initiator in the presence of a diluent, which is an organic solvent that has excellent compatibility with the monomers but is not compatible with water. Well-known methods such as suspension polymerization can be carried out, for example, as disclosed in JP-A-59-28104 and JP-A-60-165647.
By employing the method described in the publication, beads made of porous polymer can be produced.

次に、液体クロマトグラフィーによる分[濃縮法につい
て述べる。本発明に係る液体クロマトグラフィーは、公
知の高速又は工業用液体クロマトグラフィー用カラムを
用いることができ、該カラムに本発明ビーズを充填し、
脱臭留出物を注入した後、展開溶媒を通液してトコフェ
ロール類の溶出画分を分取する通常の操作で容易に目的
のトコフェロール類を得ることができる。
Next, we will discuss the concentration method using liquid chromatography. For the liquid chromatography according to the present invention, a known high-speed or industrial liquid chromatography column can be used, and the column is filled with the beads of the present invention,
After injecting the deodorized distillate, the target tocopherols can be easily obtained by the usual operation of passing a developing solvent and separating the eluted fraction of the tocopherols.

ここで展開溶媒としては、アセトン、メチルエチルケト
ン等の低級アルキルケトン類;メタノール、エタノール
、n−プロパツール、2−プロパツール等の低級アルカ
ノールM;n−ペンタン、n−へキサン、n−へブタン
、n−オクタン、イソオクタン、シクロヘキサン等の次
素数5〜8の鎖状又は環状飽和炭化水素類■イソプロピ
ルエーテル、エチ〃エーテ/I/等の低級アルキルエー
テル類、アセトニトリルv等が挙ケられ、これらの〜種
又は2楓以上を混合して用いてもよい。中でもメタノー
ル、アセトニトリルが分離濃縮性能、工業的−点等から
好ましい。
Here, the developing solvents include lower alkyl ketones such as acetone and methyl ethyl ketone; lower alkanols M such as methanol, ethanol, n-propanol, and 2-propanol; n-pentane, n-hexane, n-hebutane, Chain or cyclic saturated hydrocarbons having a prime number of 5 to 8, such as n-octane, isooctane, and cyclohexane. Lower alkyl ethers such as isopropyl ether and ethyl ether/I/, acetonitrile v, etc. ~ You may use seeds or a mixture of two or more maples. Among them, methanol and acetonitrile are preferred from the viewpoint of separation and concentration performance, industrial aspects, and the like.

(発明の効果) 本発明のポリビニル化合物を主成分とする多孔性重合体
からなるビーズを充填したカラムを用いて、液体クロマ
トグラフィーで脱臭留出物中からトコフェロール類を分
離濃縮する方法によシ、目的とするトコフェロ−/L/
pAを高純度かつ高収率でしかも効率よく分画、採取し
得、さらに本発明で用いるビーズは工業的容易に作製で
きることから安価にて高品位のトコフェロ−/L/類を
分離la網し得る点が、本発明の特筆すべき効果である
(Effect of the invention) A method for separating and concentrating tocopherols from a deodorized distillate by liquid chromatography using a column packed with beads made of a porous polymer containing the polyvinyl compound of the present invention as a main component. , target tocopherol-/L/
Since pA can be efficiently fractionated and collected with high purity and high yield, and the beads used in the present invention can be easily produced industrially, it is possible to separate high-quality tocopherols/L/s at low cost. This is a noteworthy effect of the present invention.

(実施例) 以下に実施例を示し、本発明を更に具体的に説明するが
、本発明は、かかる記載によフてその範囲を何ら限定さ
れるものではない。なお、実施例中、部及び百分率は特
に@シのない限り重上基準で示す。なお、ゲル水分率は
、脱イオン水と十分平衡にした重合体粒子を遠心効果2
000Gの遠心分離器にかけて粒子表面に付着している
水を除去したのち、その重量(Wl)を測定し、次いで
該重合体粒子を乾燥して乾燥後の重量(W2)を測定し
、次式によりて算出した。
(Examples) The present invention will be described in more detail by way of Examples below, but the scope of the present invention is not limited in any way by these descriptions. In the examples, parts and percentages are expressed on a weight basis unless otherwise noted. The gel moisture content is determined by centrifugal effect 2 of polymer particles sufficiently equilibrated with deionized water.
After removing water adhering to the particle surface by centrifuging at 000G, the weight (Wl) was measured, and then the polymer particles were dried and the dry weight (W2) was measured, and the following formula Calculated by.

実施例 1゜ メタクリル酸/p−スチレンスルホン醪ソーダー70/
30の水溶性重合体20部及びポリビニルアルコール2
部を、656部の水に溶解し、攪拌機付き1合槽に仕込
んだ。
Example 1゜Methacrylic acid/p-styrene sulfone moromi soda 70/
20 parts of water-soluble polymer of No. 30 and 2 parts of polyvinyl alcohol
1 part was dissolved in 656 parts of water, and the solution was charged into a 1-unit tank equipped with a stirrer.

剤としてエピクロルヒドリン120部の混合物に2.2
−アゾビス−(2,4−ジメチルバレロニトリル22部
を溶解して重合槽に仕込み、60cX8時間重合させた
2.2 to a mixture of 120 parts of epichlorohydrin as an agent.
-Azobis-(22 parts of 2,4-dimethylvaleronitrile was dissolved and charged into a polymerization tank, and polymerized at 60c for 8 hours.

次いで、重合液中に蟻酸5部を添加し、90CXa時間
jAI熱処理を行い、92%のゲル水分率を有する多孔
性ビーズ状重合体を作製した後、水中に分取させ沈降速
度の差で平均粒子径30μmのビーズを得た。
Next, 5 parts of formic acid was added to the polymerization solution and subjected to AI heat treatment for 90 CXa hours to produce a porous bead-like polymer having a gel moisture content of 92%. Beads with a particle size of 30 μm were obtained.

該ビーズを内径151111.長さl 000wnのカ
ラム2本に充填しこれを直列に接続し、トコフェロール
類を60%含む大豆油の脱臭留出物をメタノールで2%
溶液として該カラムに2 gg/注入した後、展開溶媒
としてメタノールを流速8゜%−y11 0 #/ /%で通液し、第1図のクロマトグラムに示
すように分画した。
The beads have an inner diameter of 151111. Packed into two columns with a length of l 000wn and connected in series, deodorized distillate of soybean oil containing 60% tocopherols was mixed with 2% methanol.
After injecting 2 gg/ml as a solution into the column, methanol was passed as a developing solvent at a flow rate of 8%-y110#/%, and fractionation was carried out as shown in the chromatogram of FIG.

その結果、目的とするα、β、r及びジ−トコフェロー
ルを純度95.2%、収率90.5%で採取した。
As a result, the target α, β, r and di-tocopherols were collected with a purity of 95.2% and a yield of 90.5%.

実施例 2゜ 実施例1.で得たビーズを内m16ax、長さ2000
絹のカラムに充填し、大豆油の脱臭留出物をアセテート
化した酢酸トコフェロール類を50%含む原料をメタノ
ールで10%浴液として該カラムに10g/注入した後
、展開mrsとし気irv てメタノールを流速3.0 m/ / ’!にで通液し
、第2図のクロマトグラムに示すように分画した。
Example 2゜Example 1. The beads obtained in the inner m16ax, length 2000
A silk column was packed, and a raw material containing 50% tocopherol acetate obtained by acetating the deodorized distillate of soybean oil was made into a 10% bath solution with methanol and 10 g/injected into the column. The flow velocity is 3.0 m//'! The mixture was passed through a chromatogram and fractionated as shown in the chromatogram in FIG.

その結果、目的とする酢酸トコフェロール類を純度96
%、収率92%で採取した。
As a result, the target tocopherol acetate was obtained with a purity of 96%.
%, with a yield of 92%.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は実施例1で、また第2図は実施例2で夫々得ら
れたクロマトグラムである。 7.10 磨 ヒ!(句I) 昭和63年 7月29日
FIG. 1 is a chromatogram obtained in Example 1, and FIG. 2 is a chromatogram obtained in Example 2. 7.10 Polish! (Phrase I) July 29, 1988

Claims (1)

【特許請求の範囲】 1、ポリビニル化合物を主成分とする多孔性重合体から
なり、該重合体の粒子径が10μ以上で、かつゲル水分
率が30%以上であるトコフェロール類の分離濃縮用ビ
ーズ。 2、油脂の脱臭工程で副生する脱臭留出物又は該脱臭留
出物をエステル化反応させた混合物中からトコフェロー
ル類を分離濃縮するに際し、請求項1記載のビーズを充
填したカラムに脱臭留出物を注入した後展開溶媒を通液
し、液体クロマトグラフィで目的とするトコフェロール
畑を分画、採取することを特徴とするトコフェロール類
の分離濃縮方法。
[Claims] 1. Beads for separating and concentrating tocopherols, which are made of a porous polymer containing a polyvinyl compound as a main component, the particle size of the polymer is 10 μ or more, and the gel moisture content is 30% or more. . 2. When separating and concentrating tocopherols from a deodorizing distillate by-produced in the deodorizing process of fats and oils or a mixture obtained by subjecting the deodorizing distillate to an esterification reaction, the deodorizing distillate is placed in a column packed with beads according to claim 1. A method for separating and concentrating tocopherols, which comprises injecting an extract, passing a developing solvent through it, and fractionating and collecting a target tocopherol field by liquid chromatography.
JP63112999A 1988-05-09 1988-05-09 Beads for separation and concentration of tocopherols and method for separation and concentration Expired - Fee Related JP2757372B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63112999A JP2757372B2 (en) 1988-05-09 1988-05-09 Beads for separation and concentration of tocopherols and method for separation and concentration

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63112999A JP2757372B2 (en) 1988-05-09 1988-05-09 Beads for separation and concentration of tocopherols and method for separation and concentration

Publications (2)

Publication Number Publication Date
JPH01284335A true JPH01284335A (en) 1989-11-15
JP2757372B2 JP2757372B2 (en) 1998-05-25

Family

ID=14600898

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Country Status (1)

Country Link
JP (1) JP2757372B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003040124A1 (en) * 2001-11-08 2003-05-15 Binder Thomas P Process for production of high purity tocopherols
KR100408991B1 (en) * 2000-03-23 2003-12-11 에스케이 주식회사 The improved method for the preparation of DL-α-tocopherol acetate

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6037110A (en) * 1983-06-21 1985-02-26 ナシヨナル・エアロノ−テイツクス・アンド・スペ−ス・アドミニストレイシヨン Insulated transformer

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6037110A (en) * 1983-06-21 1985-02-26 ナシヨナル・エアロノ−テイツクス・アンド・スペ−ス・アドミニストレイシヨン Insulated transformer

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100408991B1 (en) * 2000-03-23 2003-12-11 에스케이 주식회사 The improved method for the preparation of DL-α-tocopherol acetate
WO2003040124A1 (en) * 2001-11-08 2003-05-15 Binder Thomas P Process for production of high purity tocopherols
US6673945B2 (en) 2001-11-08 2004-01-06 Archer-Daniels Midland Company Process for production of high purity tocopherols

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