JPS59190987A - Preparation of dl-alpha-tocopherol - Google Patents

Preparation of dl-alpha-tocopherol

Info

Publication number
JPS59190987A
JPS59190987A JP6231983A JP6231983A JPS59190987A JP S59190987 A JPS59190987 A JP S59190987A JP 6231983 A JP6231983 A JP 6231983A JP 6231983 A JP6231983 A JP 6231983A JP S59190987 A JPS59190987 A JP S59190987A
Authority
JP
Japan
Prior art keywords
reaction
acetic acid
hydrochloric acid
tocopherol
ethyl acetate
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
JP6231983A
Other languages
Japanese (ja)
Other versions
JPH0559116B2 (en
Inventor
Nobuyuki Kajimoto
梶本 延之
Teruyuki Nagata
永田 輝幸
Akihiro Tamaoki
晃弘 玉置
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP6231983A priority Critical patent/JPS59190987A/en
Publication of JPS59190987A publication Critical patent/JPS59190987A/en
Publication of JPH0559116B2 publication Critical patent/JPH0559116B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To obtain the titled compound in high yield, at low temperature, by carrying out the condensation of trimethylhydroquinone with isophytol, etc. in the presence of ethyl acetate as a reaction solvent, using zinc chloride, concentrated hydrochloric acid and acetic acid as the condensation catalyst. CONSTITUTION:The objective dl-alpha-tocopherol is prepared by the condensation reaction of 2,3,5-trimethylhydroquinone with isophytol or phytol preferably at 25-30 deg.C in the presence of ethyl acetate as the reaction solvent, using zinc chloride, concentrated hydrochloric acid (preferably 35-36% concentration) and acetic acid (preferably glacial acetic acid) as the condensation catalyst. If necessary, metallic powder such as metallic zinc, iron, etc. may be added to the reaction system to suppress the generation of colored impurities produced during the reaction. The preferable molar ratio of acetic acid to hydrochloric acid is 1.5-2, that of zinc to trimethylhydroquinone is 0.8-2, and that of acetic acid and hydrochloric acid to zinc chloride is 0.3-0.5.

Description

【発明の詳細な説明】 本発明は2.3.5−トリメチルハイドロキノンと、イ
ソフィトールまたはフィトールとを反応させて、α−1
−コフエロールを製造する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides α-1
- Concerning a method for producing coferol.

従来、α−トコフェロールの製造においては、縮合触媒
として、塩化亜鉛、塩化アルミニウム、三j化ノ傾素な
どのフリデルクラフト型酸性触媒の存在下、トリメデル
ハイドロキノンとイソフィトールまたはソイ1〜−ルビ
有機溶媒を用いて、加熱還流下に反応を行うことが多数
知られている。
Conventionally, in the production of α-tocopherol, trimedelhydroquinone and isophytol or soybean chloride are combined in the presence of a Friedel-Crafts type acidic catalyst such as zinc chloride, aluminum chloride, or trij-notincline as a condensation catalyst. Many reactions are known to be carried out using organic solvents under heating and reflux.

しかしなか色、反応を高温の加熱還流下で行なえば、分
離が困難な副生物が生成し、また収率低下にもなる。
However, if the reaction is carried out at high temperature under reflux, by-products that are difficult to separate will be produced and the yield will also be reduced.

このTこめ、特開昭53−144574号公報では縮合
触媒として塩化亜鉛と塩酸を用いて、反応溶媒としてジ
クロルメタンなどのようなハロゲン化低級脂肪族炭化水
素系溶媒の存在下で、室温程度の比較的低温度で実施す
る方法が開示されている。
In this method, JP-A No. 53-144574 uses zinc chloride and hydrochloric acid as condensation catalysts, and in the presence of a halogenated lower aliphatic hydrocarbon solvent such as dichloromethane as a reaction solvent, a comparison is made at room temperature. A method is disclosed that is carried out at extremely low temperatures.

上記特開昭53−144574号方法の本発明者らの追
試ではたしかに、室温〜30”C温度でも反応Q工進み
、副生物の生成も比較的少く、良好な結果が得られるも
のの、目的生成物のα−トコフェロールはたかだか96
%の収率しか得ることができず、なお満足できるもので
なかった。
In our follow-up test of the above-mentioned method of JP-A-53-144574, it was found that the reaction progressed even at room temperature to 30"C, the production of by-products was relatively small, and good results were obtained. The amount of α-tocopherol in the product is at most 96
% yield, which was still unsatisfactory.

本発明者へは、α−トコフェロールの製造方法を鋭意検
討した結果、公知の種々の触媒及び溶媒の中から、特定
の触媒及び溶媒を選択、組み合せて使用することにより
、はからずも低温で反応させてもさ八に高収率でα−ト
コフェロールを得ることができ、工業的に満足できる方
法を見出し本発明に到達したものである。
As a result of intensive research into a method for producing α-tocopherol, the present inventor discovered that by selecting and using a specific catalyst and solvent from among various known catalysts and solvents, the reaction could be carried out at a low temperature. The present invention was achieved by discovering an industrially satisfactory method that allows α-tocopherol to be obtained in a high yield.

即ち、本発明は縮合触媒として塩化亜鉛と濃塩酸及び酢
酸を用い、反応溶媒として酢酸エチルの存在下で2.3
.5−トリメチルハイドロキノンとインフィトールまた
をエフイトールとを反応させることを。
That is, the present invention uses zinc chloride, concentrated hydrochloric acid, and acetic acid as a condensation catalyst, and in the presence of ethyl acetate as a reaction solvent.
.. Reacting 5-trimethylhydroquinone with inphytol or efytol.

特徴とするdA’−α−トコフェロールの製造方法であ
る。
This is a characteristic method for producing dA'-α-tocopherol.

本発明方法において、使用される縮合触媒は塩化亜鉛と
、濃塩酸及び酢酸が併用される。濃塩酸としては、濃度
35〜36%の塩酸が好ましく、希堪酸では収率が悪い
。また乾燥増化水素ガスを用いても差支えない。酢酸と
しては、氷酢酸が好ましく、酢酸は塩酸に一対して1〜
3モル倍、好ましくは15〜20モル倍使用する。また
酢酸及び塩酸は塩化亜鉛1モルに対し、01〜08モル
好ましく )X 0.3〜05モル量使用し、塩化亜鉛
は、トリメチルハイドロキノンエモルに対し08〜20
モル量使用する。
In the method of the present invention, the condensation catalyst used is zinc chloride in combination with concentrated hydrochloric acid and acetic acid. As concentrated hydrochloric acid, hydrochloric acid with a concentration of 35 to 36% is preferable, and dilute acid has a poor yield. Further, dry enriched hydrogen gas may also be used. As the acetic acid, glacial acetic acid is preferable;
It is used in an amount of 3 moles, preferably 15 to 20 times. In addition, acetic acid and hydrochloric acid are preferably used in an amount of 0.3 to 0.08 mol per 1 mol of zinc chloride.
Use molar amounts.

本発明において、反応温度は室温〜30℃の範囲で実施
できる。好ましくは25〜30℃に維持しなかちイソフ
ィトールまたはフィトールを滴下して酢酸エチル溶媒中
で反応を行う。
In the present invention, the reaction temperature can be in the range of room temperature to 30°C. Preferably, the temperature is maintained at 25 to 30°C, and isophytol or phytol is added dropwise to carry out the reaction in an ethyl acetate solvent.

本発明方法では、溶媒として酢酸エチルを使用する8袈
があり、縮合触媒に塩化亜鉛と酢酸及び濃塩酸を併用す
る本発明では、公知の溶媒、例えばベンゼン、1〜ルエ
ン、リグロインや、ハロゲン化脂肪族炭化水素系溶媒な
どを用いても効果は発揮できない。
In the method of the present invention, ethyl acetate is used as a solvent, and in the present invention, zinc chloride, acetic acid, and concentrated hydrochloric acid are used together as a condensation catalyst, known solvents such as benzene, 1-toluene, ligroin, and halogenated Even if aliphatic hydrocarbon solvents are used, no effect can be achieved.

また、通常α−トコフェロールの製造においては反応中
に生成する着色性不純物を抑制するため、金属亜鉛や鉄
などの金属粉末を添加して還元雰囲気下で反応を行なう
方法などが知られているが、多分その際発生する発生機
水素あるいは金属粉末と酢酸エチルとの親和性が大きい
ためか、金属粉末添加して着色副生物ノを抑制しなかへ
反応を行う場合は酢酸エチル使用による脱色効果も太き
い。しTこがって、必要あらば、反応系へ、こわらの金
属粉末を添加して実施しても差支スない。
Additionally, in order to suppress the coloring impurities generated during the reaction in the production of α-tocopherol, a method is known in which metal powders such as metallic zinc or iron are added and the reaction is carried out in a reducing atmosphere. Perhaps because of the high affinity between the generator hydrogen generated at that time or the metal powder and ethyl acetate, when the metal powder is added to suppress colored by-products and the reaction is carried out, the use of ethyl acetate also has a decolorizing effect. Thick. However, if necessary, a stiff metal powder may be added to the reaction system.

本発明方法で得へ21.た粗a−1−コフエロールは、
n法に従い、水洗、分液して、酢酸エチル油層分を蒸留
に付し、高純度の精α−トコフェロールが得へわる。
Benefits of the method of the present invention 21. The crude a-1-copherol is
After washing with water and separating the layers, the ethyl acetate oil layer was subjected to distillation to obtain highly purified purified α-tocopherol according to method N.

以下実施例を示す。Examples are shown below.

(5) 実施例1 2.3.5−トリメチルハイドロキノン125g(Q、
082モル〕、塩化亜鉛1]、2.?(0,082モル
)氷酢酸1.0 、!7 (0,017モル)、濃塩酸
(36%濃度)1.0 g (0,o 1モルフ、及び
酢酸エチル35m1を仕込み、混合攪拌下、25〜28
゛Cでイソフィトール24.5.!?(純度965%、
0080モル)を3時間で滴下した。さへに1時間攪拌
を続行し熟成反応させて反応を終了した。反応マスを水
洗し、分液後酢酸エチル油層をロータリーエバポレータ
ーにより脱溶媒濃縮し、37.ogの油状残渣(粗α−
トコフェロール)2得た。このものをGC法(注−1)
により分析しにところ、α−1−コフエロールの純度9
14%(N far )、まTこ理論収率98.1%0
対イソフイ)〜−ル)であった。
(5) Example 1 125 g of 2.3.5-trimethylhydroquinone (Q,
082 mol], zinc chloride 1], 2. ? (0,082 mol) glacial acetic acid 1.0,! 7 (0,017 mol), concentrated hydrochloric acid (36% concentration) 1.0 g (0.
Isophytol at ゛C 24.5. ! ? (965% purity,
0080 mol) was added dropwise over 3 hours. Stirring was continued for another 1 hour to cause a ripening reaction and the reaction was completed. The reaction mass was washed with water, and after separation, the ethyl acetate oil layer was desolventized and concentrated using a rotary evaporator. 37. og oily residue (crude α-
Tocopherol) 2 was obtained. GC method (Note-1)
The purity of α-1-copherol was analyzed by
14% (Nfar), theoretical yield 98.1%0
vs.

(注−1) ガスクロマトグラフィー内部標準法ビタミンE定量法に
準拠(ナショナール ホーミュラリー第14(6〕 巻) GCカラム、10%シリコンSF−301m内部標準物
質;l−’l−リアコンタン比較例1 溶媒に酢酸エチルの代りにジクロルメタンを使用した外
は、実施例1と全く同じ方法で反応及び後処理、分析を
行った。結果は次のとおりであった。
(Note-1) Based on gas chromatography internal standard method vitamin E determination method (National Homulary Vol. 14 (6)) GC column, 10% silicon SF-301m internal standard substance; l-'l-reacontane comparative example 1 solvent The reaction, post-treatment, and analysis were carried out in exactly the same manner as in Example 1, except that dichloromethane was used instead of ethyl acetate.The results were as follows.

脱溶媒後油状残渣 35.8.9 GC5法純度    90.6wt% 理論収率     9B、1% 比較例2 触媒として、塩化亜鉛と濃塩酸のみを使用して、氷酢酸
を使用しない以外は、実施例1と全く同じ方法で反応及
び後処理、分析を行った。結果は次のとおりであった。
Oily residue after desolvation 35.8.9 GC5 method purity 90.6 wt% Theoretical yield 9B, 1% Comparative Example 2 The procedure was carried out except that only zinc chloride and concentrated hydrochloric acid were used as catalysts and glacial acetic acid was not used. The reaction, post-treatment and analysis were carried out in exactly the same manner as in Example 1. The results were as follows.

脱溶媒後油状残渣 350g G、 C,法純度    89.0wt%理論収率  
   904% 比較例3 、触媒として、塩化亜鉛と氷酢酸のみを使用して、塩酸
を使用しない以外は実施例1と全く同じブ5法で反応し
Tこ。反応終了後実施例1と同様しこ水洗、分液、脱溶
媒濃縮を行つTこが、油状残渣中に固型物が析出したた
め、再び酢酸エチルを加え、酢酸エチル均一溶液としこ
ノ溶液中のd−トコフェロールを実施f1」1と同様(
こして、cc定量分析を11なった。結果(二次のとお
りであった。
Oily residue after desolvation 350g G, C, method purity 89.0wt% theoretical yield
904% Comparative Example 3 A reaction was carried out in the same manner as in Example 1 except that only zinc chloride and glacial acetic acid were used as catalysts and no hydrochloric acid was used. After completion of the reaction, washing with water, separation, and removal of solvent and concentration were carried out in the same manner as in Example 1. However, since a solid substance precipitated in the oily residue, ethyl acetate was added again to make a homogeneous ethyl acetate solution. Perform d-tocopherol in f1'' similar to 1 (
As a result, the cc quantitative analysis was 11. The results were as follows.

酢酸エチル溶液 x3o6g G、q法純度     5.11wt%理論収率   
  194% 特許出願人 三井東圧化学株式会社
Ethyl acetate solution x3o6g G, q method Purity 5.11wt% Theoretical yield
194% Patent applicant Mitsui Toatsu Chemical Co., Ltd.

Claims (2)

【特許請求の範囲】[Claims] (1)2.3.5−1〜リメチルハイl−ロキノンと、
イソフィトールまたはソイ1−−ルとを縮合させて、d
l−α〜トコフェロールを製造するに際し、縮合触媒と
して増化亜鉛と濃塩酸及び酢酸を用い、酢酸エチル反応
溶媒の存在下で反応させる、ことを特徴とするdl−α
−トコフェロールの製造方法。
(1) 2.3.5-1~limethylhy-l-quinone,
By condensing with isophytol or soil, d
l-α ~ dl-α characterized in that when tocopherol is produced, enriched zinc, concentrated hydrochloric acid and acetic acid are used as a condensation catalyst, and the reaction is carried out in the presence of an ethyl acetate reaction solvent.
- A method for producing tocopherol.
(2)酢酸を塩酸に対して、1〜3モル倍使用する特許
請求の範囲第1項記載の方法。
(2) The method according to claim 1, wherein acetic acid is used 1 to 3 times by mole relative to hydrochloric acid.
JP6231983A 1983-04-11 1983-04-11 Preparation of dl-alpha-tocopherol Granted JPS59190987A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6231983A JPS59190987A (en) 1983-04-11 1983-04-11 Preparation of dl-alpha-tocopherol

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6231983A JPS59190987A (en) 1983-04-11 1983-04-11 Preparation of dl-alpha-tocopherol

Publications (2)

Publication Number Publication Date
JPS59190987A true JPS59190987A (en) 1984-10-29
JPH0559116B2 JPH0559116B2 (en) 1993-08-30

Family

ID=13196697

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6231983A Granted JPS59190987A (en) 1983-04-11 1983-04-11 Preparation of dl-alpha-tocopherol

Country Status (1)

Country Link
JP (1) JPS59190987A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000017185A1 (en) * 1998-09-18 2000-03-30 Aventis Animal Nutrition S.A. Method for preparing vitamin e
WO2001044224A1 (en) * 1999-12-14 2001-06-21 Sk Corporation Method for preparing dl-alpha-tocopherol with a high yield and high purity
WO2002034738A1 (en) * 2000-10-23 2002-05-02 Sk Corporation Method for preparing dl-alpha-tocopherol with high yield
JP2004512332A (en) * 2000-10-23 2004-04-22 エス ケー コーポレイション Method for producing DL-α-tocopherol in high yield
CN102584770A (en) * 2011-12-31 2012-07-18 安徽丰原发酵技术工程研究有限公司 Preparation method of vitamin E
JP2013063912A (en) * 2011-08-31 2013-04-11 Eisai R & D Management Co Ltd PRODUCTION METHOD OF α-TOCOPHEROL AND ACETIC ACID α-TOCOPHEROL

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4872167A (en) * 1971-12-29 1973-09-29
JPS53103475A (en) * 1977-02-18 1978-09-08 Nisshin Flour Milling Co Ltd Preparation of highly pure d1-alpha-tocopherol
JPS53144574A (en) * 1977-05-19 1978-12-15 Eisai Co Ltd Preparation of alpha-tocopherol

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4872167A (en) * 1971-12-29 1973-09-29
JPS53103475A (en) * 1977-02-18 1978-09-08 Nisshin Flour Milling Co Ltd Preparation of highly pure d1-alpha-tocopherol
JPS53144574A (en) * 1977-05-19 1978-12-15 Eisai Co Ltd Preparation of alpha-tocopherol

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000017185A1 (en) * 1998-09-18 2000-03-30 Aventis Animal Nutrition S.A. Method for preparing vitamin e
FR2784104A1 (en) * 1998-09-18 2000-04-07 Rhone Poulenc Nutrition Animal PROCESS FOR PREPARING VITAMIN E
JP2002526489A (en) * 1998-09-18 2002-08-20 アベンテイス・アニマル・ニユートリシヨン・エス・エー Method for producing vitamin E
US6790967B2 (en) 1998-09-18 2004-09-14 Adisseo France S.A.S. Process for the preparation of vitamin E
WO2001044224A1 (en) * 1999-12-14 2001-06-21 Sk Corporation Method for preparing dl-alpha-tocopherol with a high yield and high purity
WO2002034738A1 (en) * 2000-10-23 2002-05-02 Sk Corporation Method for preparing dl-alpha-tocopherol with high yield
JP2004512332A (en) * 2000-10-23 2004-04-22 エス ケー コーポレイション Method for producing DL-α-tocopherol in high yield
JP2013063912A (en) * 2011-08-31 2013-04-11 Eisai R & D Management Co Ltd PRODUCTION METHOD OF α-TOCOPHEROL AND ACETIC ACID α-TOCOPHEROL
CN102584770A (en) * 2011-12-31 2012-07-18 安徽丰原发酵技术工程研究有限公司 Preparation method of vitamin E

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