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JPS61282357A - Production of concentrated carotene - Google Patents

Production of concentrated carotene

Info

Publication number
JPS61282357A
JPS61282357A JP12487785A JP12487785A JPS61282357A JP S61282357 A JPS61282357 A JP S61282357A JP 12487785 A JP12487785 A JP 12487785A JP 12487785 A JP12487785 A JP 12487785A JP S61282357 A JPS61282357 A JP S61282357A
Authority
JP
Japan
Prior art keywords
carotene
carotenes
acid
palm oil
adsorbent
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
JP12487785A
Other languages
Japanese (ja)
Other versions
JPS6358825B2 (en
Inventor
Hideo Mamuro
間室 秀夫
Yasuhiko Kubota
窪田 安彦
Hisako Shiina
椎名 久子
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.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP12487785A priority Critical patent/JPS61282357A/en
Publication of JPS61282357A publication Critical patent/JPS61282357A/en
Publication of JPS6358825B2 publication Critical patent/JPS6358825B2/ja
Granted legal-status Critical Current

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  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

PURPOSE:To concentrate efficiently carotene in palm oil, by treating the palm oil with a specific granular clayey adsorbent, separating the adsorbed carotene and desorbing and extracting the separated carotene with an acid and solvent. CONSTITUTION:Palm oil which may or may not be treated with polyphosphoric acid or anhydrous phosphoric acid is treated with a ganular clayey adsorbent consisting of a solid material prepared by mixing a clayey adsorbent with silicic acid gel or aluminum gel and firing the resultant mixture to adsorb and separate carotene, which is then desorbed and extracted with an organic or inorganic acid and a solvent, e.g. hexane. The solvent and acid are then removed therefrom to afford the aimed concentrated carotene, which is further brought into contact with an ion exchange resin to give the carotene with further improved concentration degree. The carotene in the palm oil as a coloring impurity is subjected to a decoloring step, but the carotene can be effectively concentrated before the step.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はパーム油を原料にしてカロテン類濃縮物を製造
する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for producing a carotene concentrate using palm oil as a raw material.

(従来の技術) パーム油中に含まれるカロテン類には主成分であるβ−
カロテンをはしめα−及びγ−カロテンなどがあり、そ
の含イ1率は、あぶらやしくオイルパーム)の品種や産
地によって異るが、0.03〜0.1%であるといわれ
ている。
(Conventional technology) Carotenes contained in palm oil contain β-
There are carotenes such as α- and γ-carotene, and their content is said to be 0.03 to 0.1%, although it varies depending on the variety and production area of the oil palm.

カロテン類はビタミンA前駆物質として生理活性を有す
ることは周知のとおりであるが、近年、ある種のがんに
対する制がん効果、抗腫瘍効果、家畜に対する排卵促進
効果などが験証されつつありこのため天然カロテン類の
濃縮法開発の機運が世界的に高まっている。
It is well known that carotenes have physiological activity as vitamin A precursors, but in recent years, their anticancer effects against certain cancers, antitumor effects, and ovulation promoting effects in livestock have been demonstrated. For this reason, there is increasing momentum around the world to develop a method for concentrating natural carotenes.

カロテン類を比較的多く含有する植物資源として人参の
根、アルファルファの葉、パーム油、海藻(Dunal
iejla  5alina)などがあげられる。なか
でもパーム油は■生産規模が大きくかつ生産量が年々増
大している、■他のカロテン含有植物資源に比べ集荷体
制が整っている、(3)カロテン類の含有率の高いパー
ム油を産生ずるあぶらやし、が品種改良によって得られ
ている、などカロテン類を型取する原料として好適であ
る (発明が解決しようとする問題点) しかしながら、パーム油に対しては従来適当な分離抽出
方法がなく、パーム油中に含まれるカロテン類は着色不
純物として、パーム油の精製工程で分解除去されている
のが現状である。
Plant resources containing relatively large amounts of carotenes include carrot root, alfalfa leaves, palm oil, and seaweed (Dunal).
iejla 5alina). Among these, palm oil is: (1) The production scale is large and the production volume is increasing year by year, (3) The collection system is better than other carotene-containing plant resources, and (3) Palm oil is produced with a high content of carotenes. The oil palm produced by palm oil is suitable as a raw material for molding carotenes, as it has been obtained through breeding. Currently, the carotenes contained in palm oil are decomposed and removed as colored impurities during the palm oil refining process.

(問題点を解決するための手段) そこで1本発明者らはパーム油の精製工程、特に脱色工
程に先立ちパーム油中に含まれるカロテン類を効果的に
e縮し得る方法を開発するため鋭意、研究を重ねた結果
、特定の粘土質吸着剤を用いることと吸着争抽出処理と
を組合わせることによりその目的を達成し得ることを見
出しこの知見に基き本発明を完成するに至った。
(Means for Solving the Problems) Therefore, the present inventors have made efforts to develop a method that can effectively e-condense carotenes contained in palm oil prior to the palm oil refining process, especially the decolorization process. As a result of repeated research, it was discovered that the objective could be achieved by combining the use of a specific clay adsorbent and an adsorption conflict extraction process, and based on this knowledge, the present invention was completed.

すなわち本発明は、パーム油又はりん酸、ポリりん酸、
もしくは無水りん酸処理をしたパーム油を、粘土質吸着
剤にケイ酸ゲル又はアルミニウムゲルを混合し焼成した
固形物からなる粒状粘土質吸着剤で処理してカロテン類
を吸着分離し、吸着分離されたカロテン類を有機酸又は
無機酸、溶媒により脱着、抽出することを特徴とする濃
縮カロテン類の調製方法を提供するものである。
That is, the present invention provides palm oil or phosphoric acid, polyphosphoric acid,
Alternatively, palm oil that has been treated with phosphoric anhydride is treated with a granular clay adsorbent consisting of a clay adsorbent mixed with silicic acid gel or aluminum gel and fired to adsorb and separate carotenes. The present invention provides a method for preparing concentrated carotenes, which is characterized by desorbing and extracting carotenes with an organic or inorganic acid or a solvent.

本発明が適用されるパーム油はパーム果肉から型取した
パーム原油(粗パーム油)、パーム原油を分別してイ1
)だ液体画分(パームオレイン)、同じく同体両分(パ
ームステアリン)などカロテン類を含有しているパーム
油である。
The palm oil to which the present invention is applied is obtained by separating crude palm oil (crude palm oil) molded from palm pulp and separating the crude palm oil.
) Palm oil contains carotenes such as a liquid fraction (palm olein) and a palm stearin fraction (palm stearin).

また、原料として、パーム油に常温又は加温Fでりん酸
、ポリりん酸、もしくは無水りん酸を接触させ、りん酸
分を分離した油分をそのまま、あるいは水洗、脱水操作
を施したのち用いてもよい。
In addition, as a raw material, palm oil is contacted with phosphoric acid, polyphosphoric acid, or phosphoric anhydride at room temperature or heated F, and the phosphoric acid content is separated and the oil is used as it is or after washing with water and dehydrating. Good too.

本発明においてこのようなパーム油を、粘土質吸着剤に
ケイ酸ゲル又はアルミニウムゲルを混合し焼成した固形
物からなる粒状粘土質吸着剤と常温又は加温下に接触さ
せて油分に含まれているカロテン類を上記粒状粘土質吸
着剤に吸着せしめる。次いで油分と吸着剤を分離する。
In the present invention, such palm oil is brought into contact with a granular clay adsorbent made of a solid material obtained by mixing a clay adsorbent with silicic acid gel or aluminum gel and calcined at room temperature or under heating to obtain the oil contained in the palm oil. The carotenes present are adsorbed onto the granular clay adsorbent. The oil and adsorbent are then separated.

この際吸着剤に付着している油分を充分取り除くことが
カロテン類の71:縮に効果的である。
At this time, sufficiently removing the oil adhering to the adsorbent is effective in reducing the amount of carotenes.

なお、りん酸、ポリりん酸、もしくは無水りん酸処理を
していないパーム油中のカロテン類を丘記粒状粘土質吸
着剤に吸着させる場合は、吸着剤の使用量を多くすれば
よい。
Note that when carotenes in palm oil that has not been treated with phosphoric acid, polyphosphoric acid, or phosphoric anhydride are to be adsorbed to the granular clay adsorbent, the amount of the adsorbent used may be increased.

パーム油、パーム油をりん酸、ポリりん酸、もしくは無
水りん酸処理をしたのちりん酸分を分離した油分、およ
び同油分に水洗、脱水操作を施したもののうちいずれの
場合でも、吸着操作を2段階に分けて行うとカロテン類
の!縮が一層効果的になされる。これは第1段の吸着操
作によりカロテン類が上記粒状粘土質吸着剤に吸着する
のを阻害する物質が除去されるためである。したがって
、第1段の吸着操作で使用する吸着剤は上記粒状粘土質
吸着剤に限らず、カロテン類がト記粒状粘ト質吸着剤に
吸着するのを阻害する物質を除去する効果を有する吸着
剤であればよい。
Adsorption operations can be performed on palm oil, palm oil treated with phosphoric acid, polyphosphoric acid, or phosphoric anhydride to separate the phosphoric acid content, and oils that have been washed with water and dehydrated. If you do it in two steps, carotenes! The shrinkage is made more effective. This is because the first stage adsorption operation removes substances that inhibit the adsorption of carotenes to the granular clay adsorbent. Therefore, the adsorbent used in the first stage adsorption operation is not limited to the granular clay adsorbent mentioned above, but also an adsorbent that has the effect of removing substances that inhibit the adsorption of carotenes to the granular viscous adsorbent described above. Any agent may be used.

油分と吸着剤を接触させる方法は、吸着剤を油分に分散
させる方法および吸着剤を充填したカラムに油分を通過
させる方法のいずれもカロテン類を上記粒状粘土質吸着
剤に吸着せしめるうえで、また、カロテン類が回吸着剤
に吸着するのを阻害する物質を除去するうえで効果的で
ある。
The methods of bringing oil into contact with the adsorbent include dispersing the adsorbent in oil and passing the oil through a column filled with the adsorbent. , is effective in removing substances that inhibit the adsorption of carotenes to the double adsorbent.

I、記粒状粘1−質吸着剤に吸着されたカロテン類は有
機酸もしくは無機酸、溶媒によって脱着、抽出するか、
その際、カロテン類が吸着している」−記粒状粘土質吸
着剤に有機酸もしくは無機酸を作用せしめ、ついで溶媒
により脱着したカロテン類を抽出する方法、カロテン類
が吸着しているl−記粒状粘度質吸着剤及び溶媒共存下
に有機酸もしくは無FjIMを添加することによりカロ
テン類を脱着、抽出する方法、及び有機酸もしくは無機
酸を含有する溶媒を用いてカロテン類を脱着、抽出する
方法のいずれも効果的である。カロテン類の抽出に用い
る溶媒はカロテン類を溶解するものであれば何でもよい
が、溶媒除去、操作を考慮すると沸点の比較的低い炭化
水素溶媒たとえばヘキサンTが好適である。
I. The carotenes adsorbed on the granular viscous adsorbent are desorbed and extracted with organic or inorganic acids or solvents, or
At that time, carotenes are adsorbed." - A method of applying an organic or inorganic acid to a granular clay adsorbent and then extracting the desorbed carotenes with a solvent. A method of desorbing and extracting carotenes by adding an organic acid or FjIM-free in the coexistence of a granular viscous adsorbent and a solvent, and a method of desorbing and extracting carotenes using a solvent containing an organic acid or an inorganic acid. Both are effective. The solvent used for extracting carotenes may be any solvent as long as it dissolves carotenes, but in consideration of solvent removal and operation, a hydrocarbon solvent with a relatively low boiling point, such as hexane T, is preferred.

カロテン類を抽出した液から溶媒及び附を除去すること
によりカロテン類の濃縮物を得る。このカロテン濃縮物
をアルコールに溶解させた溶液をイオン交換樹脂を充填
したカラムを通過させ、流出液からアルコールを除去す
ると濃縮度が一層高められたカロテン類濃縮物を得る。
A concentrate of carotenes is obtained by removing the solvent and solvent from the carotene extract. A solution of this carotene concentrate dissolved in alcohol is passed through a column filled with an ion exchange resin, and alcohol is removed from the effluent to obtain a carotene concentrate with a higher degree of concentration.

(発明の効果) 本発明によればパーム油の脱色工程に先立ち濃縮カロテ
ン類を効率的に製造することができる。
(Effects of the Invention) According to the present invention, concentrated carotenes can be efficiently produced prior to the step of decolorizing palm oil.

(実施例) 次に本発明を実施例に基づきさらに詳細に説明する。(Example) Next, the present invention will be explained in more detail based on examples.

実施例1 パーム原油300gにポリりん酸6gを加えて80°C
で1時間強くかきまぜたのち60℃に保った漏斗を用い
てろ過し、暗赤色の脂質295g、暗緑色の残留物を得
た。この脂質の可視部吸収スペクトル分析(H,A、B
ockenoogen、”Analysis  and
  Characterization  of  0
ils  Fatsand  Fat  Produc
ts”Vo12I nt erscience (19
68)9.648)結果からこの脂質にはカロテン類が
β−カロテン換算で0.034%含有されていた。この
1脂質100gを50’Cに保ちながら粘土質吸着剤に
アルミニウムゲルを混合し、焼成した固形物からなる粒
状粘土質吸着剤10gを加えて1時間かきまぜのち、脂
質と吸着剤をろ別した。吸着剤に付着している脂質はヘ
キサンで洗浄除去した。ヘキサン洗浄した吸着剤をフラ
スコに移し、酢酸5 m lとへキサン50m1を加え
、50℃に加温して吸着物を脱着、抽出した。ついで吸
着剤はヘキサン50m父で3回洗浄し、洗液は抽出液と
合せたのち、酢酸を水洗除去した。ヘキサン層は無水硫
酸ナトリウムで乾燥し、ヘキサンを減圧下に留意して0
.662gの抽出物を得た。可視部吸収スペクトルの測
定効果から、この抽出物はβ−カロテン換算で0.39
%のカロテン類を含むことを認めた。
Example 1 Add 6 g of polyphosphoric acid to 300 g of palm crude oil and heat at 80°C
After stirring vigorously for 1 hour, the mixture was filtered using a funnel kept at 60°C to obtain 295 g of dark red lipid and a dark green residue. Visible absorption spectrum analysis of this lipid (H, A, B
Ockenoogen, “Analysis and
Characterization of 0
ils Fatsand Fat Produc
ts"Vo12Int erscience (19
68)9.648) The results showed that this lipid contained 0.034% carotenes in terms of β-carotene. While maintaining 100 g of this 1 lipid at 50'C, aluminum gel was mixed with clay adsorbent, 10 g of granular clay adsorbent made of calcined solids was added, and after stirring for 1 hour, the lipid and adsorbent were separated by filtration. . Lipids adhering to the adsorbent were removed by washing with hexane. The hexane-washed adsorbent was transferred to a flask, 5 ml of acetic acid and 50 ml of hexane were added, and the mixture was heated to 50°C to desorb and extract the adsorbed material. Next, the adsorbent was washed three times with 50 ml of hexane, and the washing liquid was combined with the extract, and the acetic acid was removed by washing with water. The hexane layer was dried over anhydrous sodium sulfate, and the hexane was carefully removed under reduced pressure.
.. 662 g of extract was obtained. From the measurement effect of the visible absorption spectrum, this extract has a content of 0.39 in terms of β-carotene.
% of carotenes.

実施例2 実施例工で得た抽出物0.53gを50m1のメタノー
ルに溶解した溶液を、あらかじめ活性化しておいたアン
バーライト401型アニオン交換樹脂5gを充填したガ
ラス塔を通過させ、流出した液からメタノールを留去し
て0.018gの流出画分を得た。可視部吸収スペクト
ル分析の結果、この流出画分にはβ−カロテン換算で1
0.8%のカロテン類が存在していることを認めた。
Example 2 A solution in which 0.53 g of the extract obtained in the example process was dissolved in 50 ml of methanol was passed through a glass column filled with 5 g of Amberlite 401 type anion exchange resin that had been activated in advance, and the liquid that flowed out was Methanol was distilled off to obtain a 0.018 g effluent fraction. As a result of visible absorption spectrum analysis, this effluent fraction contained 1
The presence of 0.8% carotenes was observed.

実施例3 パーム原油液体画分(パームオレイン)300gに無水
りん酸粉末6gを加え80℃で1時間かきまぜた。無水
りん醜をろ別したのち油分を水洗脱水して293gの油
分を得た。この油分に0.5重量%の活性白土を加え、
50’(!で1時間処理した。この処理油は可視吸収ス
ペクトル分析の結果、β−カロテン換算で0.055%
のカロテン類を含んでいた。
Example 3 6 g of phosphoric anhydride powder was added to 300 g of palm crude oil liquid fraction (palm olein) and stirred at 80° C. for 1 hour. After filtering off the anhydrous phosphorus, the oil was washed with water and dehydrated to obtain 293 g of oil. Add 0.5% by weight of activated clay to this oil,
50' (!) for 1 hour. This treated oil was 0.055% in terms of β-carotene as a result of visible absorption spectrum analysis
Contains carotenes.

活性白土処理油100gに、粘土質吸着剤にシリカゲル
を混合し焼成した粒状粘土質吸着剤10gを加え、50
℃で1時間かきまぜてカロテン類を吸着剤に吸着させた
。カロテン類ヂ吸着した吸着物を脱着、抽出し、0.7
5gの抽出物を得た。IIT視部吸収スペクトル分析の
結果、この抽出物は、β−カロテン換算で0.98%の
カロテン類を含んでいた。
To 100 g of activated clay treated oil, 10 g of granular clay adsorbent mixed with silica gel and calcined was added.
The mixture was stirred at ℃ for 1 hour to allow the carotenes to be adsorbed onto the adsorbent. Desorb and extract the adsorbate that adsorbed carotenes, 0.7
5g of extract was obtained. As a result of IIT optical absorption spectrum analysis, this extract contained 0.98% carotenes in terms of β-carotene.

実施例4 実施例3で得た抽出物0.6gをエタノール50mMに
溶かした溶液を実施例2と同様にしてイオン交換樹脂と
接触させ、流出液からエタノールを除去し、0.036
gの暗かっ色の粘稠物質を得た。445nmにおける吸
光度から、この粘稠物質にはβ−カロテン換算で11.
5%のカロテン類が存在していることを認めた。
Example 4 A solution prepared by dissolving 0.6 g of the extract obtained in Example 3 in 50 mM ethanol was brought into contact with an ion exchange resin in the same manner as in Example 2, and ethanol was removed from the effluent.
g of a dark brown viscous substance was obtained. Based on the absorbance at 445 nm, this viscous substance contains 11.0% in terms of β-carotene.
The presence of 5% carotenes was observed.

特許出願人 工業技術院長 等々労連 ・二、パ・;・ひり゛。Patent applicant: Director of the Agency of Industrial Science and Technology, Todoro Federation ・Second, Pa;・Hiri゛.

手 続 補 正 書(自発) 60化技研第1172号 昭和 6ン7月23−日 特許庁長官 宇賀 道部 殿  、− vしジ 1、事件の表示  昭和60年特許願第 124877
  号2、発明の名称  濃縮カロテン類の調製方法3
、補正をする者 事件との関係特許出願人 住 所    東京都千代田区霞が関1丁目3番1号’
re″’tb  (114)工業技術院長  等々力 
  達(発送日    昭和  年  月  日)8、
 補正の内容 本願明細書中において)次の通り補正します。
Procedural Amendment (Spontaneous) No. 60 Kagiken No. 1172, June 1985, July 23, 1984 - Mr. Michibe Uga, Commissioner of the Patent Office, v. Shiji 1, Indication of Case Patent Application No. 124877 of 1985
No. 2, Title of the invention Method for preparing concentrated carotenes 3
Address of the patent applicant related to the person making the amendment: 1-3-1 Kasumigaseki, Chiyoda-ku, Tokyo'
re'''tb (114) Todoroki, Director of the Agency of Industrial Science and Technology
(Shipping date: Showa, month, day) 8,
Contents of the amendment The following amendments will be made in the specification of the application.

(1)  第2頁下から第2行の「するあぶらやし1が
」を「するあぶらやしが」に訂正します。
(1) In the second line from the bottom of the second page, ``Suru oil palm 1 ga'' is corrected to ``Suru oil palm ga''.

(2)  第3頁第3行の「パーム油に対しては10.
」を「パーム油中のカロテン類に対しては01.」に訂
正します。
(2) Page 3, line 3, “10.
" will be corrected to "01. for carotenes in palm oil."

(3)  第6頁第7行〜第8行の「ついで溶媒により
脱着したカロテン類を10.」を「ついで脱着したカロ
テン類を溶媒により61.」に訂正します。
(3) On page 6, lines 7 and 8, "Then, the carotenes desorbed by the solvent are 10." is corrected to "Then, the carotenes desorbed by the solvent are 61.".

(4)  第6頁下から第6行の「溶媒除去A操作」を
「溶媒除去操作」に訂正します。
(4) Correct "Solvent removal A operation" in the 6th line from the bottom of page 6 to "Solvent removal operation."

(5)  第8頁下から第8行の「下に留意して01.
」を「下に留去して00.」に訂正します。
(5) On page 8, line 8 from the bottom, “01.
" is corrected to "00."

Claims (2)

【特許請求の範囲】[Claims] (1)パーム油又はりん酸、ポリりん酸、もしくは無水
りん酸処理をしたパーム油を、粘土質吸着剤にケイ酸ゲ
ル又はアルミニウムゲルを混合し焼成した固形物からな
る粒状粘土質吸着剤で処理してカロテン類を吸着分離し
、吸着分離されたカロテン類を有機酸又は無機酸、溶媒
により脱着、抽出することを特徴とする濃縮カロテン類
の調製方法。
(1) Palm oil or palm oil treated with phosphoric acid, polyphosphoric acid, or phosphoric anhydride is used as a granular clay adsorbent consisting of a solid substance obtained by mixing silicic acid gel or aluminum gel with clay adsorbent and firing the mixture. 1. A method for preparing concentrated carotenes, which comprises treating and adsorbing and separating carotenes, and desorbing and extracting the adsorbed and separated carotenes with an organic or inorganic acid or a solvent.
(2)抽出分離したカロテン類をさらにイオン交換樹脂
と接触させることを特徴とする特許請求の範囲第1項記
載の濃縮カロテン類の調製方法。
(2) The method for preparing concentrated carotenes according to claim 1, characterized in that the extracted and separated carotenes are further brought into contact with an ion exchange resin.
JP12487785A 1985-06-08 1985-06-08 Production of concentrated carotene Granted JPS61282357A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12487785A JPS61282357A (en) 1985-06-08 1985-06-08 Production of concentrated carotene

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12487785A JPS61282357A (en) 1985-06-08 1985-06-08 Production of concentrated carotene

Publications (2)

Publication Number Publication Date
JPS61282357A true JPS61282357A (en) 1986-12-12
JPS6358825B2 JPS6358825B2 (en) 1988-11-17

Family

ID=14896301

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12487785A Granted JPS61282357A (en) 1985-06-08 1985-06-08 Production of concentrated carotene

Country Status (1)

Country Link
JP (1) JPS61282357A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003530367A (en) * 2000-04-05 2003-10-14 ヘルガソン・ハフスタイン Compound recovery method using natural adsorbent
WO2006090871A1 (en) * 2005-02-25 2006-08-31 Yamaha Hatsudoki Kabushiki Kaisha Method of recovering xanthophyll
GB2511086A (en) * 2013-02-22 2014-08-27 Shayonano Singapore Pte Ltd Process For The Isolation of Carotenoids

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003530367A (en) * 2000-04-05 2003-10-14 ヘルガソン・ハフスタイン Compound recovery method using natural adsorbent
WO2006090871A1 (en) * 2005-02-25 2006-08-31 Yamaha Hatsudoki Kabushiki Kaisha Method of recovering xanthophyll
GB2511086A (en) * 2013-02-22 2014-08-27 Shayonano Singapore Pte Ltd Process For The Isolation of Carotenoids
WO2014129974A1 (en) * 2013-02-22 2014-08-28 Shayonano Singapore Pte Ltd Process for the isolation of carotenoids
CN105026368A (en) * 2013-02-22 2015-11-04 莎尤纳诺新加坡私人有限公司 Process for the isolation of carotenoids
US9592499B2 (en) 2013-02-22 2017-03-14 Shayonano Singapore Pte Ltd Process for the isolation of carotenoids

Also Published As

Publication number Publication date
JPS6358825B2 (en) 1988-11-17

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