JPS6019309B2 - Production method of high purity dl-α-tocopherol - Google Patents

Production method of high purity dl-α-tocopherol

Info

Publication number
JPS6019309B2
JPS6019309B2 JP11596576A JP11596576A JPS6019309B2 JP S6019309 B2 JPS6019309 B2 JP S6019309B2 JP 11596576 A JP11596576 A JP 11596576A JP 11596576 A JP11596576 A JP 11596576A JP S6019309 B2 JPS6019309 B2 JP S6019309B2
Authority
JP
Japan
Prior art keywords
tocopherol
high purity
purity
production method
present
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
JP11596576A
Other languages
Japanese (ja)
Other versions
JPS5344570A (en
Inventor
雄二郎 吉野
和子 近藤
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.)
Nisshin Seifun Group Inc
Original Assignee
Nisshin Seifun Group 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 Nisshin Seifun Group Inc filed Critical Nisshin Seifun Group Inc
Priority to JP11596576A priority Critical patent/JPS6019309B2/en
Priority to DE19772743920 priority patent/DE2743920C2/en
Publication of JPS5344570A publication Critical patent/JPS5344570A/en
Priority to US06/011,882 priority patent/US4217285A/en
Publication of JPS6019309B2 publication Critical patent/JPS6019309B2/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D311/00Heterocyclic compounds containing six-membered rings having one oxygen atom as the only hetero atom, condensed with other rings
    • C07D311/02Heterocyclic compounds containing six-membered rings having one oxygen atom as the only hetero atom, condensed with other rings ortho- or peri-condensed with carbocyclic rings or ring systems
    • C07D311/04Benzo[b]pyrans, not hydrogenated in the carbocyclic ring
    • C07D311/58Benzo[b]pyrans, not hydrogenated in the carbocyclic ring other than with oxygen or sulphur atoms in position 2 or 4
    • C07D311/70Benzo[b]pyrans, not hydrogenated in the carbocyclic ring other than with oxygen or sulphur atoms in position 2 or 4 with two hydrocarbon radicals attached in position 2 and elements other than carbon and hydrogen in position 6
    • C07D311/723,4-Dihydro derivatives having in position 2 at least one methyl radical and in position 6 one oxygen atom, e.g. tocopherols

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Pyrane Compounds (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Description

【発明の詳細な説明】 本発明はdl−Qートコフェロールの製造法に関し、さ
らに詳しくはトリメチルハィドロキノンとフィトール類
とを、シリカアルミナおよび/またはシリカゲル、塩化
亜鉛およびプロトン酸の存在下で反応させることによっ
て高純度dl−Qートコフェロールを製造する方法に関
する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing dl-Q tocopherol, and more particularly, the present invention relates to a method for producing dl-Q tocopherol. The present invention relates to a method for producing high purity dl-Q tocopherol by.

従来dl−Qートコフェロールの製造法としては有機溶
媒中p−トルェンスルホン酸等のプロトン酸触媒、塩化
亜鉛等のルイス酸触媒あるいはシリカァルミナ等の固体
酸触媒のもとで縮合させる方法が知られている。
Conventionally, known methods for producing dl-Q tocopherol include condensation in an organic solvent under a protonic acid catalyst such as p-toluenesulfonic acid, a Lewis acid catalyst such as zinc chloride, or a solid acid catalyst such as silica alumina. ing.

しかしながらこれらの方法によってdl−Q−トコフヱ
ロールを製造した場合、副生物が生成する欠点がある。
そしてこの創生物は繰り返し精製処理を行っても除去す
ることができなかった。従って従来法にあってはdl−
Q−トコフェロールアセテートに関するアメリカ国民医
薬品集の規格(Natio佃IFonnula14ed
ition)に定める96%以上の純度を有する製品を
商業的に得ることは、高真空蒸留を繰り返すことによっ
ても不可能に近かった。発明者等は高純度dinq−ト
コフヱロールを製造する方法について種々研究を重ねた
結果高純度dl−Q−トコフェロールを得る方法を見出
した。
However, when dl-Q-tocopherol is produced by these methods, there is a drawback that by-products are produced.
This created organism could not be removed even after repeated purification treatments. Therefore, in the conventional method, dl-
American National Formulary Standards for Q-Tocopherol Acetate (Natio Tsukuda IFonnula 14ed
It has been nearly impossible to commercially obtain a product with a purity of 96% or higher, as defined in the US Pat. The inventors conducted various studies on methods for producing high-purity dinq-tocopherol, and as a result, they discovered a method for obtaining high-purity dl-Q-tocopherol.

本発明方法は前記したようにトリメチルハィドロキノン
とフイトール類とをシリカアルミナおよび/またはシリ
カゲル、塩化亜鉛およびプロトン酸の存在下に縮合させ
る方法に関する。本発明の原料物質の一つであるフィト
ール類としてはフィトールの外、ィソフイトールあるい
はフイチルクロライド、フイチルブロマイドの如きハラ
イド類、フイチルアセテート、フイチルプロピオネート
の如きアルキルェステル類等の反応性誘導体も使用する
ことができる。また本発明方法に使用されるプロトン酸
としては塩酸、硫酸、りん酸、p−トルェンスルホン酸
等が挙げられるが、特に塩酸が好ましい。反応溶媒とし
てはnーヘキサン、ィソオクタン、石油エーテル等の脂
肪族炭化水素、ベンゼン、トルェン、キシレン等の芳香
族炭化水素、シクoヘキサン、テトラリン等の脂環式化
合物、四塩化炭素のハロゲン化炭化水素、ジオキサン等
の環状エーテル等の極性の低い溶媒〔譲亀率(2030
)3以下のもの〕を使用すると特に好ましい結果が得ら
れる。本発明方法を実施するに当って使用するシリカア
ルミナ、シリカゲルおよび塩化亜鉛は必要に応じてそれ
ぞれ焼成乾燥してもよい。
The method of the present invention, as described above, relates to a method of condensing trimethylhydroquinone and phytols in the presence of silica alumina and/or silica gel, zinc chloride and protonic acid. In addition to phytol, the phytols that are one of the raw materials of the present invention include isophytol, halides such as phytyl chloride and phytyl bromide, and alkyl esters such as phytyl acetate and phytyl propionate. Sexual derivatives can also be used. Examples of protonic acids used in the method of the present invention include hydrochloric acid, sulfuric acid, phosphoric acid, p-toluenesulfonic acid, and the like, with hydrochloric acid being particularly preferred. Reaction solvents include aliphatic hydrocarbons such as n-hexane, isooctane, and petroleum ether, aromatic hydrocarbons such as benzene, toluene, and xylene, alicyclic compounds such as cyclohexane and tetralin, and halogenated hydrocarbons such as carbon tetrachloride. , low polarity solvents such as cyclic ethers such as dioxane [Yield rate (2030
) 3 or less], particularly favorable results are obtained. The silica alumina, silica gel and zinc chloride used in carrying out the method of the present invention may be dried by calcination, if necessary.

シリカアルミナおよび/またはシリカゲルの使用量はト
リメチルハイドロキ・ノンと同量程度使用することが好
ましく、また塩化亜鉛は触媒量の使用でよい。さらにプ
ロトン酸はフイトール類の0.5〜5.0%程度を添加
することが好ましい。反応条件は原料、溶媒および触媒
の組合せにより一定しないが、通常は50〜120qo
、1〜5時間程度で十分であるが、特にこれらの範囲に
限定されるものではない。反応生成物は例えば反応混合
物を水洗、アルカリ水洗族し、溶媒を脱水処理した後必
要に応じてアセチル化した後高真空蒸留することにより
精製することができる。本発明方法によれば、粗dl−
Q−トコフェロールアセテートを−回の真空蒸留を行う
だけで高純度dl−Q−トコフェリルアセテートを得る
ことができ、商業的に極めて有利な方法と云える。
The amount of silica alumina and/or silica gel used is preferably about the same amount as that of trimethylhydroquinone, and zinc chloride may be used in a catalytic amount. Furthermore, it is preferable to add protonic acid in an amount of about 0.5 to 5.0% of the phytols. Reaction conditions vary depending on the combination of raw materials, solvents and catalysts, but usually 50 to 120 qo
, about 1 to 5 hours is sufficient, but is not particularly limited to these ranges. The reaction product can be purified, for example, by washing the reaction mixture with water, washing with alkali water, dehydrating the solvent, acetylating if necessary, and then performing high vacuum distillation. According to the method of the present invention, crude dl-
High purity dl-Q-tocopheryl acetate can be obtained by simply subjecting Q-tocopherol acetate to two rounds of vacuum distillation, and this method can be said to be commercially extremely advantageous.

本発明方法の優位性を示すために従来方法と対比すると
下記のとおりである。まずイソフィトール25.0夕、
トリメチルハイドロキノン13.5夕、シリカアルミナ
またはシリカゲル13.5夕、塩化亜鉛6.0夕よびプ
ロトン酸0.5夕を使用して縮合させ、得られたdl−
Q−トコフェロールを常法によってアセチル化した後真
空蒸留により16.5〜175qo/8×10‐3脚H
gの区分を分取した。なお純度測定はnードトリアコン
タンを内部標準としたガスクロマトグラフイ一によった
。以下にその試験結果を第1表に示す。第1表 次に本発明方法を具体的に説明するために実施例を挙げ
るが、本発明は以下の実施例に限定されるものではない
In order to show the superiority of the method of the present invention, a comparison with the conventional method is as follows. First, isophytol 25.0 pm,
The resulting dl-
After acetylating Q-tocopherol by a conventional method, 16.5 to 175 qo/8×10-3 leg H was obtained by vacuum distillation.
A fraction of g was collected. The purity was measured by gas chromatography using n-dotriacontane as an internal standard. The test results are shown in Table 1 below. Table 1 Examples will be given to specifically explain the method of the present invention, but the present invention is not limited to the following examples.

実施例 1 トリメチルハイドロキノン13.5夕をトルヱンloo
叫に溶解し、窒素気流下にシリカアルミナ13.5夕、
塩化亜鉛6.0夕および濃塩酸(35%塩酸)0.5夕
を加え、反応系を85午0に加温した後イソフィトール
25.0夕を約20分間で滴下する。
Example 1 Trimethylhydroquinone 13.5% to toluene
Silica alumina was dissolved in a nitrogen stream for 13.5 min.
After adding 6.0 mm of zinc chloride and 0.5 mm of concentrated hydrochloric acid (35% hydrochloric acid) and warming the reaction system to 85:00, 25.0 mm of isophytol was added dropwise over about 20 minutes.

滴下後同温度で約4時間蝿梓を続けた後放袷する。次に
反応物にトルェン100の‘を加えて混合する。不溶物
を炉過し、炉液を3%苛性ソーダ‐1%ハイドロサルフ
アィトソーダ混液、水、飽和食塩水で順次洗い、無水硫
酸マグネシウムで脱水した後溶媒を減圧留去しdl−Q
ートコフヱロール37.0夕を得る(収率99.8%)
。次に得られたdl−Q−トコフェロール25.0夕を
無水酢酸50の【に溶解し、酢酸ナトリウム12.5夕
および金属亜鉛末1.25夕を加え、95〜100oo
で約3.虫時間燈枠を行ってアセチル化した後、n−へ
キサン200の‘を加えて抽出し、抽出液を1%苛性ソ
ーダ、水、飽和食塩水で順次,洗い、硫酸マグネシウム
で乾燥後nーヘキサンを減圧留去して粗dl−Qートコ
フェリルアセテート26.2夕を得る。次に得られた粗
dl−Qートコフェリルアセテートを真空蒸留し、16
5〜175午0ノ8×10‐3肋Hgの本蟹区分20.
5夕を得る。このものの純度は97.3%であり、蒸留
収率は78.0%である。実施例 2トリメチルハィド
After dropping, the mixture was kept at the same temperature for about 4 hours and then released. Next, 100% of toluene is added to the reactants and mixed. Insoluble matter was filtered through a furnace, and the furnace liquid was washed sequentially with a mixture of 3% caustic soda and 1% hydrosulfite soda, water, and saturated saline, and after dehydration over anhydrous magnesium sulfate, the solvent was distilled off under reduced pressure to obtain dl-Q.
Obtained 37.0 tons of tocopherol (yield 99.8%)
. Next, 25.0 g of the obtained dl-Q-tocopherol was dissolved in 50 g of acetic anhydride, 12.5 g of sodium acetate and 1.25 g of metal zinc powder were added, and 95 to 100 g of dl-Q-tocopherol was dissolved.
Approximately 3. After acetylation by diaphragm, extraction was performed by adding 200% of n-hexane, and the extract was sequentially washed with 1% caustic soda, water, and saturated saline, dried over magnesium sulfate, and extracted with n-hexane. Distillation under reduced pressure yields 26.2 g of crude dl-Q tocopheryl acetate. Next, the obtained crude dl-Q tocopheryl acetate was vacuum distilled, and 16
5-175 pm 0 no 8 x 10-3 ribs Hg classification 20.
Get 5 evenings. The purity of this product is 97.3%, and the distillation yield is 78.0%. Example 2 Trimethylhide.

キノン13.5夕を四塩化炭素10物上に分散させ、窒
素気流下にシリカゲル13.5塩化亜鉛6.0夕および
濃塩酸(35%塩酸)0.5夕を加え、反応系を780
0に加溢した後ィソフィトール類25.0夕を約2び分
間で滴下する。滴下後同温度で約4時間櫨梓を続けた後
放冷する。反応物に四塩化炭素100叫を加えて混合す
る。
13.5% of quinone was dispersed over 10% of carbon tetrachloride, 13.5% of silica gel, 6.0% of zinc chloride and 0.5% of concentrated hydrochloric acid (35% hydrochloric acid) were added under a nitrogen stream to reduce the reaction system to 780%.
After flooding with 0.0 ml, 25.0 ml of isophytol was added dropwise over about 2 minutes. After dropping, the mixture was kept at the same temperature for about 4 hours, and then allowed to cool. Add 100 ml of carbon tetrachloride to the reactants and mix.

不溶物を炉遇し、炉液を3%苛性ソーダ一1%ハイドロ
サルフアイドソーダ混液、水、飽和食塩水で順次洗い、
無水硫酸マグネシウムで脱水した後溶媒を減圧留去して
dl−Q−トコフェロール36.0夕を得る(収率99
.1%、純度95.3%)。次に得られたdl−Qート
コフェロール25.0夕を無水酢酸50の【に溶解し、
これに酢酸ナトリウム12.5夕および金属亜鉛末1.
25夕を加え、95〜100℃で約3.曲時間燈洋を行
ってアセチル化した後目的生成物を・1ーヘキサン20
0の‘を加えて抽出する。抽出液を1%苛性ソーダ、水
、飽和食塩水で順次洗い、硫酸マグネシウムで乾燥後、
n−へキサンを減圧留去して粗dl−Q−トコフェリル
アセテート25.8夕を得る。次に得られた粗dl−Q
−トコフェリルアセテートを真空蒸留し165〜175
『0/8×10‐3皿Hgの本蟹区分19.6夕を得る
(蒸留収率76.0%、純度96.8%)。
The insoluble matter was heated in a furnace, and the furnace solution was washed sequentially with a mixture of 3% caustic soda and 1% hydrosulfide soda, water, and saturated saline.
After dehydration over anhydrous magnesium sulfate, the solvent was distilled off under reduced pressure to obtain 36.0 g of dl-Q-tocopherol (yield: 99.
.. 1%, purity 95.3%). Next, 25.0 g of the obtained dl-Q tocopherol was dissolved in 50 g of acetic anhydride,
To this was added 12.5 tons of sodium acetate and 1.5 tons of metal zinc powder.
Add 25 days of heat and heat at 95-100℃ for about 3. After acetylation by performing a periodic process, the desired product was converted into 1-hexane 20
Extract by adding 0'. The extract was washed sequentially with 1% caustic soda, water, and saturated saline, and dried over magnesium sulfate.
The n-hexane was distilled off under reduced pressure to obtain 25.8 g of crude dl-Q-tocopheryl acetate. Then the crude dl-Q obtained
-Vacuum distillation of tocopheryl acetate 165-175
``0/8 x 10-3 plate Hg of 19.6 pieces of real crab were obtained (distillation yield 76.0%, purity 96.8%).

Claims (1)

【特許請求の範囲】[Claims] 1 トリメチルハイドロキノンとフイトール類とをシリ
カアルミナおよび/またはシリカゲル、塩化亜鉛および
プロトン酸の存在下で縮合させることを特徴とする高純
度dl−α−トコフエロールの製造法。
1. A method for producing high purity dl-α-tocopherol, which comprises condensing trimethylhydroquinone and phytols in the presence of silica alumina and/or silica gel, zinc chloride and protonic acid.
JP11596576A 1976-09-29 1976-09-29 Production method of high purity dl-α-tocopherol Expired JPS6019309B2 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP11596576A JPS6019309B2 (en) 1976-09-29 1976-09-29 Production method of high purity dl-α-tocopherol
DE19772743920 DE2743920C2 (en) 1976-09-29 1977-09-29 Process for the preparation of dl-α-tocopherol
US06/011,882 US4217285A (en) 1976-09-29 1979-02-13 Process for the preparation of Dl-α-tocopherol of high purity

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11596576A JPS6019309B2 (en) 1976-09-29 1976-09-29 Production method of high purity dl-α-tocopherol

Publications (2)

Publication Number Publication Date
JPS5344570A JPS5344570A (en) 1978-04-21
JPS6019309B2 true JPS6019309B2 (en) 1985-05-15

Family

ID=14675511

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11596576A Expired JPS6019309B2 (en) 1976-09-29 1976-09-29 Production method of high purity dl-α-tocopherol

Country Status (2)

Country Link
JP (1) JPS6019309B2 (en)
DE (1) DE2743920C2 (en)

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4256251A (en) * 1978-04-24 1981-03-17 Lawrence M. Smith Surgical staplers and staple
JPS5615407A (en) * 1979-07-19 1981-02-14 Asahi Chem Ind Co Ltd Pot
JPS5615406A (en) * 1979-07-19 1981-02-14 Asahi Chem Ind Co Ltd Spinning pot
DE3203487A1 (en) * 1982-02-03 1983-08-11 Basf Ag, 6700 Ludwigshafen METHOD FOR PRODUCING TOCOPHERYL ACETATE OR TOCOPHERYL PROPIONATE
JPH01183513A (en) * 1988-01-19 1989-07-21 Toho Rayon Co Ltd Pot for spinning
DE4208477A1 (en) * 1992-03-17 1993-09-23 Basf Ag METHOD FOR PRODUCING VITAMIN E
DE4243464A1 (en) * 1992-12-22 1994-06-23 Basf Ag Process for the preparation of alpha-tocopherol and alpha-tocopheryl acetate in liquid or supercritical carbon dioxide
DE19524928A1 (en) * 1995-07-08 1997-01-09 Basf Ag Process for the rectification of mixtures of high-boiling air and / or temperature sensitive substances, which require a high separation performance, in a fine vacuum, as well as columns suitable for this process
US6005122A (en) * 1996-12-23 1999-12-21 Basf Aktiengesellschaft Preparation of α-tocopherol or α-tocopheryl acetate by reacting trimethylhydroquinone and phytol or isophytol, with recycling of the zinc halide condensation catalyst
KR100710546B1 (en) * 1999-07-13 2007-04-24 에스케이 주식회사 Method for preparing DL-alpha-Tocopherol with high yield
KR100452291B1 (en) * 1999-12-14 2004-10-08 에스케이 주식회사 Method for preparing DL-α-tocopherol with a high yield and purity
CN1186337C (en) * 2000-10-23 2005-01-26 Sk株式会社 Method for preparing Dl-alpha-to copherol with high yield
KR20020042176A (en) * 2000-11-30 2002-06-05 유승렬 Method for preparing DL-α-tocopherol with a high yield and high purity
DE602005027081D1 (en) 2004-08-19 2011-05-05 Dsm Ip Assets Bv METHOD FOR THE RECTIFICATION OF VITAMIN E ACETATE
CN101006070B (en) 2004-08-19 2012-11-07 帝斯曼知识产权资产管理有限公司 Process for the working-up of a vitamin e- and vitamin e-acetate-containing mixture or product stream

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3708505A (en) * 1971-02-25 1973-01-02 Diamond Shamrock Corp Process for preparation of d,l-alpha tocopherol

Also Published As

Publication number Publication date
DE2743920C2 (en) 1984-10-18
DE2743920A1 (en) 1978-03-30
JPS5344570A (en) 1978-04-21

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