JPS59227876A - Separation of tocopherols - Google Patents
Separation of tocopherolsInfo
- Publication number
- JPS59227876A JPS59227876A JP10149983A JP10149983A JPS59227876A JP S59227876 A JPS59227876 A JP S59227876A JP 10149983 A JP10149983 A JP 10149983A JP 10149983 A JP10149983 A JP 10149983A JP S59227876 A JPS59227876 A JP S59227876A
- Authority
- JP
- Japan
- Prior art keywords
- distillate
- tocopherols
- acid
- oil
- deacidified
- 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
Links
Landscapes
- Pyrane Compounds (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、植物油の脱酸留出物及び脱臭留出物から、ト
コフェロール類を分離する方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for separating tocopherols from deoxidized and deodorized distillates of vegetable oils.
天然トコフェロール類の生産原料として、従来から、植
物油の脱酸留出物又は脱臭留出物が用いられている。こ
れらの原料からトコフェロール類を分離する過程で、蒸
留及び有機溶剤処理等の操作があり、その間、トコフェ
ロール類の酸化、重合及び分解等が起り、その含有量が
低下する。そこで、トコフェロール類の分離濃縮工程中
で、トコフェロール含有量の低下を防止する方法の開発
が要望されている。Deoxidized distillates or deodorized distillates of vegetable oils have conventionally been used as raw materials for producing natural tocopherols. In the process of separating tocopherols from these raw materials, operations such as distillation and treatment with organic solvents are performed, during which oxidation, polymerization, decomposition, etc. of tocopherols occur, resulting in a decrease in their content. Therefore, there is a need for the development of a method for preventing a decrease in tocopherol content during the separation and concentration process of tocopherols.
本発明はトコフェロール類を含有する大豆油の脱臭留出
物、米ぬか油脱臭留出物及びパーム油留出脂肪酸等から
トコフェロール類の酸化及び重合等を防止しながら、分
離する方法に関するものである。The present invention relates to a method for separating tocopherols from a deodorized distillate of soybean oil, a deodorized rice bran oil distillate, a palm oil distillate fatty acid, etc. containing tocopherols while preventing oxidation and polymerization of the tocopherols.
本発明においては、植物油の脱酸留出物又は脱臭留出物
をメチルエステル化処理する際に、食品用酸化防止剤を
添加し、通常の方法によりメチルエステル化を行う。次
に、メチルエステルを蒸留除去する場合には食品用酸化
防止剤を加えた後蒸留を行う。さらに、トコフェロール
類が濃縮された蒸留残留物に食品用酸化防止剤を加えた
後、分子蒸留を行い、留出物として、原料中のトコフェ
ロール類の80%以上が、濃縮物中に含まれる。In the present invention, when a deoxidized distillate or a deodorized distillate of vegetable oil is subjected to methyl esterification treatment, a food grade antioxidant is added and methyl esterification is performed by a conventional method. Next, when removing methyl ester by distillation, distillation is performed after adding a food grade antioxidant. Furthermore, after adding a food-grade antioxidant to the distillation residue in which tocopherols are concentrated, molecular distillation is performed, and as a distillate, 80% or more of the tocopherols in the raw material are contained in the concentrate.
本発明で使用する食品用酸化防止剤は、食品用天然酸化
防止剤として例えばアスコルビン酸、レシチン、コーヒ
ー酸、フェル/7酸工ステル等及ヒ食品用合成酸化防止
剤として、例えばブチルヒドロキシアニソール、ノルジ
ヒドログアヤレチック酸等がある。これらの酸化防止剤
の使用量はそれそれに応じた適量があるが、大体重量比
2チ以下、る。The food-grade antioxidants used in the present invention include natural food-grade antioxidants such as ascorbic acid, lecithin, caffeic acid, fer/7-acid esters, etc., and food-grade synthetic antioxidants such as butylhydroxyanisole, Examples include nordihydroguaiaretic acid. The amount of these antioxidants to be used is determined depending on the situation, but the weight ratio should be less than 2%.
次に、本発明を実施例によりさらに詳細に説明する。Next, the present invention will be explained in more detail with reference to Examples.
実施例1゜
パーム油蒸留脂肪酸1 kgにL−アスコルビン酸0.
4g、塩酸15 voよ%を含むメタ/−ルl、27を
加え、窒素気流下500〜60℃で2時間、かきまぜ、
反応物を水洗、脱水、口過してメチルエステル化物1.
1kgを得た。Example 1 1 kg of palm oil distilled fatty acid was added with 0.0.0 kg of L-ascorbic acid.
4g of hydrochloric acid, 15% of hydrochloric acid, 27% was added, and stirred at 500 to 60°C for 2 hours under a nitrogen stream.
The reaction product was washed with water, dehydrated, and passed through the mouth to obtain the methyl ester compound 1.
1 kg was obtained.
ついで、このメチルエステル化物の減圧蒸留(tOTo
rr )を行ない、180℃までに留出するメチルエス
テルを蒸留除去した。蒸留留出物89.2チ、残留物1
0.8%。この残留物中には原料パーム油蒸留脂肪酸中
に含まれるトコフェロール及びトコトリエノール類の約
80%が濃縮されていた。Then, this methyl ester product was distilled under reduced pressure (tOTo
rr) to remove the methyl ester distilled out up to 180°C. Distillate: 89.2 cm, residue: 1
0.8%. Approximately 80% of the tocopherols and tocotrienols contained in the raw palm oil distilled fatty acid were concentrated in this residue.
これに対しL−アスコルビン酸を加えずに同様な処理を
行なった場合は約40%しか濃縮されな751つだ。On the other hand, if the same treatment was performed without adding L-ascorbic acid, the concentration would be only about 40% (751).
実施例2゜
米ぬか油脱臭留出物(トコフェロール濃度1.86%)
に、IO,1%のアスコルビン酸を添加し、水酸化
ナトリウム5.5%メタノール溶液を加えて窒素気流下
室温で15分間攪拌する。次に、塩酸メタノール溶液で
酸性とし、エーテルを加えた後に水洗を行う。得られた
脂肪酸混合物中のトコフェロール濃度は196%であっ
た。このものに再び0.1チアスコルビン酸を添加し、
塩酸メタノール溶液を加えて窒素気流下40°Cで1時
間攪拌する。エーテルを加えて水洗いし、得られた脂肪
酸メチルエステル混合物中のトコフェロール濃度は1.
90%、回収率は93.5%であった。Example 2゜Rice bran oil deodorized distillate (tocopherol concentration 1.86%)
To this, IO, 1% ascorbic acid is added, and a 5.5% methanol solution of sodium hydroxide is added, followed by stirring at room temperature for 15 minutes under a nitrogen stream. Next, the mixture is made acidic with a methanol solution of hydrochloric acid, and ether is added, followed by washing with water. The tocopherol concentration in the resulting fatty acid mixture was 196%. Add 0.1 thiascorbic acid to this again,
Add a methanol solution of hydrochloric acid and stir at 40°C for 1 hour under a nitrogen stream. After adding ether and washing with water, the tocopherol concentration in the fatty acid methyl ester mixture obtained was 1.
The recovery rate was 90% and 93.5%.
次に、このものを、l’I’orr以下で減圧蒸留する
と、残渣が56チ得られた。トコフェロール濃度は3.
40%で回収率は原料の米ぬか油脱臭留出物と比べて9
3.4チであった。Next, this product was distilled under reduced pressure below 1'I'orr to obtain 56 residues. Tocopherol concentration is 3.
The recovery rate is 40%, which is 9% compared to the raw material rice bran oil deodorized distillate.
It was 3.4 chi.
実施例3
パーム油の脱酸及び脱臭工程で得られる留出脂肪e ]
、 kgに、アスコルビン酸0.1g、ブチルヒドロキ
シアニソール0,1g及びクエン酸0.21を添加後、
2チ濃硫酸を含有するメタノールl kgを加え、60
℃で3時間かきまぜた。次に、水洗、脱水後、1 ’p
orr、180℃以下の留分を除去し、残留物55gを
得た。Example 3 Distillate fat e obtained in palm oil deacidification and deodorization process]
, after adding 0.1 g of ascorbic acid, 0.1 g of butylated hydroxyanisole and 0.21 g of citric acid to
2 kg of methanol containing concentrated sulfuric acid was added, and 60
Stir at ℃ for 3 hours. Next, after washing with water and dehydrating, 1'p
The fraction below 180°C was removed to obtain 55 g of residue.
この残留物に0.3■のアスコルビン酸とメタノール5
Qmlを加えて、60℃、10分かきまぜた。This residue contains 0.3 μ of ascorbic acid and 5 μm of methanol.
Qml was added and stirred at 60°C for 10 minutes.
室温に放置して、メタノール区分を分別した。同様ノメ
タノール処理を3回繰返し、メタノール区分を分取した
。メタノール区分はロータリーエバポレーターを用いて
、メタノールを留去し、残留物7.51を得た。It was left at room temperature and the methanol fraction was separated. The same nomethanol treatment was repeated three times, and the methanol fraction was collected. For the methanol fraction, methanol was distilled off using a rotary evaporator to obtain a residue of 7.51.
この残留物中のトコフェロール類の含有量は3.4gで
、原料の留出脂肪酸中のトコフェロール含有量の85%
に相当する。The content of tocopherols in this residue is 3.4 g, which is 85% of the tocopherol content in the distilled fatty acid as the raw material.
corresponds to
上記のトコフェロール分離過程で酸化防止剤を添加しな
い場合には、残留物中のトコフェロール類、2.4gで
原料の留出脂肪酸中のトコフェロール含有量の40係で
あった。When no antioxidant was added in the above tocopherol separation process, the tocopherols in the residue were 2.4 g, which was 40 times the tocopherol content in the distilled fatty acid as the raw material.
実施例4
米ぬか油の脱臭工程で得られる留出物2 kgに1多水
酸化ナトリウムを含有するメタノール500m1と0.
1.9のブチルヒドロキシアニソール60℃で、1時間
加熱後、未反応のメタノールを留去した。残留物を温水
で水洗した。次に、2チ硫酸−メタノール500m1と
017i(Dブチルヒドロキシアニソールを残留物に加
え、1時間、還流加熱した。加熱後ロータリーエバポレ
ーターを用いて、過剰のメタノールを留去した。残留物
を水洗、脱水後、l’porr、180℃以下の留分を
除去し、残留物1.050gを得た。Example 4 2 kg of distillate obtained in the deodorizing process of rice bran oil was mixed with 500 ml of methanol containing 1.
After heating at 60° C. for 1 hour, unreacted methanol was distilled off. The residue was washed with warm water. Next, 500 ml of dithiosulfuric acid-methanol and 017i (D-butylhydroxyanisole) were added to the residue and heated under reflux for 1 hour. After heating, excess methanol was distilled off using a rotary evaporator. The residue was washed with water, After dehydration, the fraction below 180° C. was removed to obtain 1.050 g of residue.
この残留物にメタノール21と0.05gのプチルヒド
ロキシアlソールを加え、60℃、10分間かンを50
0 all加え、−20°Cの冷蔵庫に一東放置した。To this residue was added methanol 21 and 0.05 g of butylated hydroxyalsol, and the mixture was heated at 60°C for 10 minutes at 50°C.
0 all were added and left in a refrigerator at -20°C.
生成した結晶をロ別腰ロ液部143Iを得た。A liquid portion 143I was obtained from the generated crystals.
この口液部のトコフェロール量は61.6gで原料の留
出物中のトコフェロール量の88%になる。The amount of tocopherol in this oral fluid portion was 61.6 g, which was 88% of the amount of tocopherol in the raw material distillate.
Claims (1)
ールを抽出又は濃縮する場合に食品用酸化防止剤を添加
する方法。(1) A method of adding a food grade antioxidant when extracting or concentrating tocopherols and tocotrienols from natural products.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10149983A JPS6020389B2 (en) | 1983-06-07 | 1983-06-07 | Separation method of tocopherols |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10149983A JPS6020389B2 (en) | 1983-06-07 | 1983-06-07 | Separation method of tocopherols |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59227876A true JPS59227876A (en) | 1984-12-21 |
JPS6020389B2 JPS6020389B2 (en) | 1985-05-21 |
Family
ID=14302324
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10149983A Expired JPS6020389B2 (en) | 1983-06-07 | 1983-06-07 | Separation method of tocopherols |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6020389B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1065433C (en) * | 1992-06-22 | 2001-05-09 | 丹羽笑代 | Oily preparation and method of production thereof |
KR100884570B1 (en) | 2005-03-07 | 2009-02-18 | 순천향대학교 산학협력단 | A method of mass-production tocotrienol in rice bran and bran-based functional foodstuff containing tocotrienol with high content |
-
1983
- 1983-06-07 JP JP10149983A patent/JPS6020389B2/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1065433C (en) * | 1992-06-22 | 2001-05-09 | 丹羽笑代 | Oily preparation and method of production thereof |
KR100884570B1 (en) | 2005-03-07 | 2009-02-18 | 순천향대학교 산학협력단 | A method of mass-production tocotrienol in rice bran and bran-based functional foodstuff containing tocotrienol with high content |
Also Published As
Publication number | Publication date |
---|---|
JPS6020389B2 (en) | 1985-05-21 |
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