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JPS6015627B2 - Production method of α-tocopherol - Google Patents
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JPS6015627B2 - Production method of α-tocopherol - Google Patents

Production method of α-tocopherol

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Publication number
JPS6015627B2
JPS6015627B2 JP747376A JP747376A JPS6015627B2 JP S6015627 B2 JPS6015627 B2 JP S6015627B2 JP 747376 A JP747376 A JP 747376A JP 747376 A JP747376 A JP 747376A JP S6015627 B2 JPS6015627 B2 JP S6015627B2
Authority
JP
Japan
Prior art keywords
tocopherol
yield
purity
solvent
reaction
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.)
Expired
Application number
JP747376A
Other languages
Japanese (ja)
Other versions
JPS5291865A (en
Inventor
静正 貴島
吉三郎 浜村
優介 小西
豊 森
千秋 関
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.)
Eisai Co Ltd
Original Assignee
Eisai 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 Eisai Co Ltd filed Critical Eisai Co Ltd
Priority to JP747376A priority Critical patent/JPS6015627B2/en
Publication of JPS5291865A publication Critical patent/JPS5291865A/en
Publication of JPS6015627B2 publication Critical patent/JPS6015627B2/en
Expired legal-status Critical Current

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  • Pyrane Compounds (AREA)

Description

【発明の詳細な説明】 本発明は、Q−トコフェロールの製造法に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing Q-tocopherol.

さらに詳しくは、2・3・5ートリメチルー1・4ーハ
イドロキノンと、フイトール及び/又はィソフイトール
とを、塩化亜鉛を触媒として縮合せしめてQートコフヱ
ロールを製造する方法に関するものである。従来、Qー
トコフェロールの製造法として、2・3・5−トリメチ
ルー1・4ーハイドロキノンとフイトール及び/又はィ
ソフィトールを縮合せしめるに際し、塩化亜鉛を結合剤
として使用し、リグロイン、テトラリン、ベンゼン、ト
ルェン、キシレンなどの脂肪族あるいは芳香族炭化水素
系溶媒中で加熱還流する方法が知られている。しかし、
これら従来方法では加熱還流と云う苛酷な反応条件が必
須であるため、往々にして副反応が生じ、フィチルダィ
マー等の高沸点化合物が創生する。これら高潔点化合物
は蒸留による精製操作では除去困難で、ガスクロマトグ
ラフ上あるいは薄層クロマトグラフ上これら高沸点化合
物の狭雑のない純度の高いQ−トコフェロールを得るた
めには、縮合反応生成物の蒸留精製操作における蟹出範
囲を厳密にコントロールしなければならず、目的物Q−
トコフェロール収率低下の大きい原因となっている。本
発明者等は、従来のQートコフェロール製造法の上託せ
る欠点を解除して高純度のQートコフェロールを収率よ
く製造すべく研究し、本発明の方法によって所期の目的
が蓮せられる事を確認した。
More specifically, the present invention relates to a method for producing Q tocopherol by condensing 2,3,5-trimethyl-1,4-hydroquinone with phytol and/or isophytol using zinc chloride as a catalyst. Conventionally, as a method for producing Q tocopherol, zinc chloride is used as a binder when condensing 2,3,5-trimethyl-1,4-hydroquinone with phytol and/or isophytol, and ligroin, tetralin, benzene, toluene, A method of heating under reflux in an aliphatic or aromatic hydrocarbon solvent such as xylene is known. but,
Since these conventional methods require severe reaction conditions such as heating under reflux, side reactions often occur and high-boiling compounds such as phytyl dimer are created. These high-point compounds are difficult to remove by purification by distillation, and in order to obtain highly pure Q-tocopherol without the contamination of these high-boiling point compounds on gas chromatography or thin layer chromatography, it is necessary to distill the condensation reaction product. It is necessary to strictly control the extraction range during refining operations, and the target product Q-
This is a major cause of a decrease in tocopherol yield. The present inventors have conducted research to eliminate the drawbacks of conventional Q-tocopherol production methods and produce high-purity Q-tocopherol in good yield, and have achieved the intended purpose by the method of the present invention. I confirmed that it is possible.

本発明の方法は2・3・5−トリメチルー1・4ーハイ
ドロキノンとフイトール及び/又はイソフイトールとを
塩化亜鉛を触媒として縮合反応せしめてQートコフェロ
ールを製造するに際して、反応溶媒として低級脂肪族ハ
ロゲン化炭化水素系溶媒と低級脂肪族エーテル系溶媒と
の混合溶媒を使用してはートコフェロールを製造する事
からなる。
The method of the present invention involves the condensation reaction of 2,3,5-trimethyl-1,4-hydroquinone with phytol and/or isophytol using zinc chloride as a catalyst to produce Q tocopherol, in which lower aliphatic halogenation is used as a reaction solvent. Tocopherol is produced using a mixed solvent of a hydrocarbon solvent and a lower aliphatic ether solvent.

本発明の方法において使用される低級脂肪族ハロゲン化
炭化水素系溶媒としては、例えばジクロルメタン、クロ
ロホルム、四塩化炭素、エチレンジクロラィド等を挙げ
る事ができる。低級脂肪族エーテル系溶媒としては、例
えばジメチルェーテル、ジエチルエーテル、エチルメチ
ルエーナル、ジプロピルエーテル、ジイソプロピルエー
ナル、ジーnーブチルェーテルを挙げる事ができる。上
記溶媒において、ジクロルメタンーイソブロピルェーテ
ル混合溶媒の使用が特に好ましい結果を与えた。本発明
の方法の利点は、縮合反応を行なうに際して加熱還流を
行なう必要のない事で、そのため従釆法の欠点である高
沸点化合物の創生が殆どなく、縮合生成物を常法に従っ
て分子蒸留した場合、純度97%以上〔ナショナル ホ
ーミュラリー(NatjoMIFo側ulary)第1
4登第7斑〜762頁記載のガスクロマト法によるビタ
ミンE定量法に従って測定した。
Examples of the lower aliphatic halogenated hydrocarbon solvent used in the method of the present invention include dichloromethane, chloroform, carbon tetrachloride, and ethylene dichloride. Examples of lower aliphatic ether solvents include dimethyl ether, diethyl ether, ethyl methyl ether, dipropyl ether, diisopropyl ether, and di-n-butyl ether. Among the above solvents, the use of a dichloromethane-isopropylether mixed solvent gave particularly favorable results. The advantage of the method of the present invention is that there is no need to heat reflux when carrying out the condensation reaction, so there is almost no generation of high-boiling compounds, which is a drawback of the conventional method, and the condensation product is subjected to molecular distillation using a conventional method. If the purity is 97% or more [National Homulary (NatjoMIFo side ulary) 1st
It was measured according to the vitamin E quantitative method using the gas chromatography method described on page 762 of No. 4, No. 7.

以下同じ〕のQートコフェロールが88%以上の収率で
得られると云う高結果をもたらした。また従来法に比較
して高沸点化合物の狭雑が少ない事は、ガスクロマトグ
ラフ上あるいは薄層クロマトグラフ上にても確認された
。以上より本発明は、従来法に比してより高純度のQー
トコフェロールを、より高収率で提供する事をその目的
とするものとする。
The same results hereinafter] were obtained in a yield of 88% or more. It was also confirmed on a gas chromatograph or thin layer chromatograph that the concentration of high boiling point compounds was less than in the conventional method. From the above, it is an object of the present invention to provide Q tocopherol with higher purity and higher yield than conventional methods.

次に実施例および比較例により本発明を説明する。Next, the present invention will be explained with reference to Examples and Comparative Examples.

なお目的物Qートコフェロールの純度は前記したナショ
ナル ホーミュラリー第14坂記載のガスクロマト法に
従って測定した。実施例 1 2・3・5−トリメチルー1・4−ハイドロキノン7.
8夕(0.05モル)、無水塩化亜鉛6.8夕0.05
モル)をジクロルメタン20の‘、ジイソプロピルエー
テル5の‘の混合溶媒に加え、更に氷酢酸1叫を加えた
のち、室温にて櫨梓下にィソフィトール(純度95%)
15.6夕(0.05モル)を3時間を要して滴下し、
滴下終了後、更に30分間同一条件下で縄拝した。
The purity of the target substance Q tocopherol was measured according to the gas chromatography method described in National Homulary No. 14, mentioned above. Example 1 2,3,5-trimethyl-1,4-hydroquinone7.
8 mol (0.05 mol), anhydrous zinc chloride 6.8 mol 0.05
After adding 1 mol of dichloromethane and 5 mol of diisopropyl ether to a mixed solvent of 1 mol of dichloromethane and 5 mol of diisopropyl ether, add isophytol (purity 95%) at room temperature.
15.6 moles (0.05 mol) was added dropwise over 3 hours,
After the dropping was completed, the rope was bowed under the same conditions for an additional 30 minutes.

反応終了後、溶媒を減圧留去して得られる赤褐色油状物
をn−へキサン150泌に溶解し、水、2%水酸化ナト
リウ水溶液、飽和食塩水にて順次洗修し、苦硝で乾燥し
たのち、溶媒を減圧蟹去した。赤燈色油状物質(粗Qー
トコフェロール)22.1夕を得た。収率99%(ィソ
フイトールを基として)純度 95% この赤燈色油状物質を分子蒸留に附して無色油状物質(
精製Qートコフヱロール)18.9夕を得た。
After the reaction, the solvent was distilled off under reduced pressure, and the resulting reddish brown oil was dissolved in 150% n-hexane, washed successively with water, 2% aqueous sodium hydroxide, and saturated brine, and dried with bitter salt. Thereafter, the solvent was removed under reduced pressure. 22.1 hours of a red light oil (crude Q-tocopherol) was obtained. Yield 99% (based on isophytol) purity 95% This reddish oil is subjected to molecular distillation to produce a colorless oil (
Purified Q-tocopherol) 18.9 hours was obtained.

収率88%純度 99% 実施例 2 2・3・5ートリメチル−1・4ーハイドロキノン7.
8夕、イソフイトール156夕、糠水塩化亜鉛5.6夕
、氷酢酸1の‘をジクロルメタン20泌、ジェチルェー
テル3の‘の浪合溶媒を使用し、実施例1に従って反応
処理した。
Yield 88% Purity 99% Example 2 2,3,5-trimethyl-1,4-hydroquinone7.
After 8 days, reaction treatment was carried out according to Example 1 using a mixture of 156 times of isophytol, 5.6 times of bran water zinc chloride, 1 part of glacial acetic acid, 20 parts of dichloromethane, and 3 parts of diethyl ether.

粗Q−トコフェロール:赤燈色油状物質 収量 21.9夕(収率98%) 純度 93% 精製Q−トコフェロール:無色油状物質 収量 181夕(収率滋%) 純度 98% 実施例 3 2・3・5−トリメチルー1・4−ハイドロキノン7.
8夕、ィソフィトール15.6夕、無水塩化亜鉛6.8
夕、氷酢酸1の‘をヱチレンジクロラィド20泌、ジイ
ソプロピルェーテル5の‘の混合溶媒を使用し実施例1
に従って反応処理した。
Crude Q-tocopherol: Reddish oily substance Yield: 21.9 hours (yield: 98%) Purity: 93% Purified Q-tocopherol: Colorless oily substance: Yield: 181 hours (yield: 98%) Purity: 98% Example 3 2-3・5-trimethyl-1,4-hydroquinone 7.
8 evenings, isophytol 15.6 evenings, anhydrous zinc chloride 6.8 evenings
In the evening, Example 1 was prepared using a mixed solvent of 1 part of glacial acetic acid, 20 parts of ethylene dichloride, and 5 parts of diisopropyl ether.
The reaction was carried out according to the following.

粗Q−トコフェロール:赤燈色油状物質 収量 22.2夕(収率99%) 純度 92% 精製Qートコフヱロール:無色油状物質 収量 18.8夕(収率84%) 純度 聡% 実施例 4 2・3・5−トリメチル−1・4ーハイドロキノン7.
82、ィソフィトール15.6夕、無水塩化亜鉛5.6
夕、氷酢酸1泌を1・1・1ートリクロルェタン20舷
、ジーnーブチルェーテル3の‘の混合溶媒を使用し、
実施例1に従って反応処理した。
Crude Q-tocopherol: Reddish oily substance Yield 22.2 hours (yield 99%) Purity 92% Purified Q-tocopherol: Colorless oily substance Yield 18.8 hours (yield 84%) Purity Satoshi% Example 4 2. 3,5-trimethyl-1,4-hydroquinone7.
82, isophytol 15.6%, anhydrous zinc chloride 5.6%
In the evening, using a mixed solvent of 1 part of glacial acetic acid, 20 parts of 1,1,1-trichloroethane, and 3 parts of di-butyl ether,
The reaction was carried out according to Example 1.

粗Q−トコフェロール:赤燈色油状物質収量 21.8
夕(収率職%) 純度 94% 精製Qートコフェロール:無色油状物質 収量 18.5夕(収率86%) 純度 斑% 実施例 5 2・3・5−トリメチルー1・4ーハイドロキノン11
4夕(0.7モル)、イソフイトール234夕(0.7
5モル)、無水塩化亜鉛105夕、氷酢酸15の‘を1
・1ージク0ルエタン300のと、ジイソプロピルェー
テル75叫の混合溶媒を使用し、実施例1に従って反応
処理した。
Crude Q-tocopherol: Red light oil yield 21.8
Purity (yield %) Purity 94% Purified Q-tocopherol: colorless oil Yield 18.5 (yield 86%) Purity Spot % Example 5 2,3,5-trimethyl-1,4-hydroquinone 11
4 moles (0.7 mol), isophytol 234 moles (0.7 mol)
5 moles), 105 parts of anhydrous zinc chloride, 1 part of glacial acetic acid
- A reaction treatment was carried out according to Example 1 using a mixed solvent of 300 parts of 1-dichloroethane and 75 parts of diisopropyl ether.

粗q−トコフェロール:赤燈色油状物質 収量 332夕(収率99.4%) 純度 94% この粗Qートコフェロール332のこ無水酢酸193夕
、酢酸ナトリウム滋夕、亜鉛末2.4夕、トルェン25
0心を加え2時間燈拝下に加熱還流し、反応終了後、反
応液を放冷、次いで氷水1〆中に注ぎ入れ、有機溶媒層
を分取し、水洗、芝硝にて乾燥したのち、溶媒を減圧留
去した。
Crude q-tocopherol: reddish oily substance Yield: 332 ml (yield 99.4%) Purity: 94% This crude q-tocopherol: 332 ml, acetic anhydride: 193 ml, sodium acetate, zinc powder: 2.4 ml, toluene 25
Add zero core, heat under reflux for 2 hours under light, and after the reaction is complete, the reaction solution is left to cool, then poured into ice water. The organic solvent layer is separated, washed with water, and dried with Shiba Glass. , the solvent was distilled off under reduced pressure.

殆ど無色の油状物質はートコフェリル アセテート36
4夕を得た。収率99.5%これを分子蒸留して精製Q
ートコフェリル アセテート320夕を得た。
The almost colorless oily substance is tocopheryl acetate 36
I got 4 nights. Yield 99.5% This was purified by molecular distillation Q
Tocopheryl acetate 320mg was obtained.

本品の純度は聡2%であつた。比較例 1 実施例1においてジイソブロピルェーテルを使用しない
他は同様の操作を行ない、精製Q−トコフェロールを得
た。
The purity of this product was 2% Satoshi. Comparative Example 1 Purified Q-tocopherol was obtained by carrying out the same operation as in Example 1 except that diisopropylether was not used.

黄赤色油状物質 20.8夕(収率93%)純度 78
%比較例 2 実施例1においてジィソプロピルェーテル25の‘だけ
を使用して、ジクロルメタンを使用しない他は同様の操
作を行ない、精製Q−トコフヱロールを得た。
Yellow-red oil 20.8 min (yield 93%) Purity 78
% Comparative Example 2 Purified Q-tocopherol was obtained by carrying out the same operation as in Example 1 except that only diisopropyl ether 25' was used and dichloromethane was not used.

黄色油状物質 20.2夕(収率91%)純度 62%Yellow oil 20.2 hours (yield 91%) Purity 62%

Claims (1)

【特許請求の範囲】[Claims] 1 2・3・5−トリメチル−1・4−ハイドロキノン
と、フイトール及び/又はイソフイトールとを、塩化亜
鉛を触媒として縮合反応せしめてα−トコフエロールを
製造するに際して、反応触媒として低級脂肪族ハロゲン
化炭化水素系溶媒と低級脂肪族エーテル系溶媒との混合
溶媒を使用する事を特徴とする、α−トコフエロールの
製造法。
1 When producing α-tocopherol by condensation reaction of 2,3,5-trimethyl-1,4-hydroquinone and phytol and/or isophytol using zinc chloride as a catalyst, lower aliphatic halogenated carbonization is used as a reaction catalyst. A method for producing α-tocopherol, characterized by using a mixed solvent of a hydrogen solvent and a lower aliphatic ether solvent.
JP747376A 1976-01-28 1976-01-28 Production method of α-tocopherol Expired JPS6015627B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP747376A JPS6015627B2 (en) 1976-01-28 1976-01-28 Production method of α-tocopherol

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP747376A JPS6015627B2 (en) 1976-01-28 1976-01-28 Production method of α-tocopherol

Publications (2)

Publication Number Publication Date
JPS5291865A JPS5291865A (en) 1977-08-02
JPS6015627B2 true JPS6015627B2 (en) 1985-04-20

Family

ID=11666746

Family Applications (1)

Application Number Title Priority Date Filing Date
JP747376A Expired JPS6015627B2 (en) 1976-01-28 1976-01-28 Production method of α-tocopherol

Country Status (1)

Country Link
JP (1) JPS6015627B2 (en)

Also Published As

Publication number Publication date
JPS5291865A (en) 1977-08-02

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