JPS60120828A - Production of bisabolol - Google Patents

Production of bisabolol

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Publication number
JPS60120828A
JPS60120828A JP22826583A JP22826583A JPS60120828A JP S60120828 A JPS60120828 A JP S60120828A JP 22826583 A JP22826583 A JP 22826583A JP 22826583 A JP22826583 A JP 22826583A JP S60120828 A JPS60120828 A JP S60120828A
Authority
JP
Japan
Prior art keywords
reaction
bisabolol
formic acid
nerolidol
mixture
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
JP22826583A
Other languages
Japanese (ja)
Other versions
JPS6365052B2 (en
Inventor
Hironobu Tamai
洋進 玉井
Tomoyuki Aya
綾 友幸
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.)
Kuraray Co Ltd
Original Assignee
Kuraray 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 Kuraray Co Ltd filed Critical Kuraray Co Ltd
Priority to JP22826583A priority Critical patent/JPS60120828A/en
Publication of JPS60120828A publication Critical patent/JPS60120828A/en
Publication of JPS6365052B2 publication Critical patent/JPS6365052B2/ja
Granted legal-status Critical Current

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

PURPOSE:To obtain industrially and advantageously the aimed compound, by carrying out cyclization reaction in a specific nonpolar solvent in producing bisabolol useful as an anti-inflammatory agent, etc., by cyclizing nerolidol in the presence of formic acid, and if necessary hydrolyzing the reaction product. CONSTITUTION:3,7,11-Trimethyldodeca-1,6,10-trien-3-ol (nerolidol) is cyclized in a nonpolar solvent, preferably hexane, heptane, cyclopentane, cyclohexane, ethylcyclohexane, benzene, toluene or xylene having <=3.0 dielectric constant measured at 20 deg.C in the presence of formic acid preferably at about 0-50 deg.C, and the resultant reaction product is if necessary hydrolyzed to afford the aimed bisabolol in high yield. According to the method, formic acid with up to about 30wt% moisture content can be used, and the formic acid after recovery can be reused. The reaction is easily controlled.

Description

【発明の詳細な説明】 本発明はビサボロールの製造方法に関し、詳しくは3,
7.11− )リメチルドデカー1.6.10− )ジ
エン−5−オール(ネロリドール)をギ酸の存在下に環
化させ、ついで必要に応じて該生成物を加水分解してビ
サボロールを製造するに際し、該環化反応を誘電率3.
0以下の非極性溶媒の存在下に行なうことを特徴とする
ビサボロールの製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing bisabolol, and in detail, 3.
7.11-) Limethyldodecar 1.6.10-) Dien-5-ol (nerolidol) is cyclized in the presence of formic acid and then optionally hydrolyzed to produce bisabolol. , the cyclization reaction is carried out with a dielectric constant of 3.
The present invention relates to a method for producing bisabolol, characterized in that it is carried out in the presence of a non-polar solvent of 0 or less.

ビサボロールはカミツレ油、ラベンダー油などに存在し
ている単環式不飽和第3級セスキテルペンアルコールで
あり、抗炎症及び抗菌作用を有し、軟膏、クリーム、ロ
ーションなどの皮膚治療製品又は歯みがき、うがい薬な
どの口腔衛生用品に使用されているばかりでなく、保香
性を有することから調合香料の保留剤としても使用され
ている。
Bisabolol is a monocyclic unsaturated tertiary sesquiterpene alcohol that is present in chamomile oil, lavender oil, etc., and has anti-inflammatory and antibacterial properties, and can be used in skin treatment products such as ointments, creams, and lotions, or in toothpaste and gargles. It is not only used in oral hygiene products such as medicines, but also as a preservative for mixed fragrances because of its fragrance-retaining properties.

ビサボロールの合成法としてネロリドール又はファルネ
ソールをギ酸の存在下に環化させ、ついでその生成物を
加水分解させる方法が知られている。この方法における
環化反応について、C,D。
A known method for synthesizing bisabolol is to cyclize nerolidol or farnesol in the presence of formic acid and then hydrolyze the product. Regarding the cyclization reaction in this method, C, D.

GUTSCHEらはギ酸に対して数重量%という非常に
希薄な状態のファルネソール又はネロリドールを用いて
、反応時間、反応温度、ギ酸の含水率及び原料アルコー
ルの相異が環化反応の速度、生成物組成に与える影響を
検討し、(1)ネロリドールはファルネソールよりも速
く環化すること、(2)純度100%のギ酸を使用した
場合に反応速度が最も大きく、ギ酸の含水率が高くなる
につれて反応速度が急激に低下すること、(3)純度1
00チのギ酸を使用した場合、反応温度30℃では反応
が非常に速く、反応開始後わずか1分間でビサボロール
、ビサボレンなどの単環生成物の生成量は最大となり、
時間の経過とともにその生成量は減少すること、これに
付随してビサボロール及び/又はそのギ酸エステルの生
成量も減少すること、 (4) )ランス、トランス−
ファルネソールを純度100%のギ酸の存在下に反応さ
せた場合、反応温度0°Cではビサボロール及び/又は
そのギ酸エステルの生成量は約5分後に最大量に達し、
その後減少するが、生成物中のビサボロール、ビサボレ
ンなどの単環生成物の総濃度は急激に増加し、約10分
後に最大限に達すること等を報告している( Tet−
rahedron、 Vol、24. pp、 859
〜876 (1968)参照〕。
GUTSCHE et al. used farnesol or nerolidol in a very dilute state of several percent by weight relative to formic acid, and found that differences in reaction time, reaction temperature, water content of formic acid, and starting alcohol were used to determine the rate of the cyclization reaction and the product yield. We examined the effects on the composition and found that (1) nerolidol cyclizes faster than farnesol; (2) the reaction rate is highest when 100% pure formic acid is used, and as the water content of formic acid increases, (3) Purity 1
When 00% formic acid is used, the reaction is very fast at a reaction temperature of 30°C, and the amount of monocyclic products such as bisabolol and bisabolene produced reaches its maximum in just 1 minute after the start of the reaction.
(4)) Lance, trans-
When farnesol is reacted in the presence of 100% pure formic acid, at a reaction temperature of 0°C, the amount of bisabolol and/or its formate ester produced reaches the maximum amount after about 5 minutes.
After that, it decreases, but the total concentration of monocyclic products such as bisabolol and bisabolene in the product increases rapidly, reaching the maximum after about 10 minutes (Tet-
rahedron, Vol, 24. pp, 859
~876 (1968)].

また本発明者らはこの従来法を種々の反応条件下で検討
したところ、純度75チ(含水率25重量%)のギ酸を
使用してネpリドールを環化させた場合には転化率2O
4程度で殆んど反応が進行しなくなるとの知見を得た。
In addition, the present inventors investigated this conventional method under various reaction conditions and found that when nepridol was cyclized using formic acid with a purity of 75% (water content 25% by weight), the conversion rate was 20%.
It was found that the reaction hardly progresses at a temperature of about 4.

このように、上記の従来法は反応の制御が難しいこと、
また高純度のギ酸を必要とすること、さらにこの環化反
応を行なう場合には副反応である脱水反応及び生成した
ビサボロールとギ酸とのエステル化反応による水の生成
を避けることができず、しかも水とギ酸とは共沸組成を
形成することから、生成した水を含みかつ反応に大量に
使用されたギ酸を回収後、再使用するには厳密な脱水精
製工程が必要となること等、工業的な製造方法としては
採用し難い問題点を有する。
In this way, the above conventional methods have difficulties in controlling the reaction;
In addition, highly purified formic acid is required, and when performing this cyclization reaction, it is impossible to avoid the side reactions of dehydration and the production of water due to the esterification reaction between the bisabolol and formic acid produced. Since water and formic acid form an azeotropic composition, a rigorous dehydration and purification process is required in order to recover and reuse the formic acid that contains produced water and was used in large quantities in the reaction. This method has problems that make it difficult to adopt as a standard manufacturing method.

本発明者らはネロリドールをギ酸の存在下に環化させ、
ついで必要に応じて該生成物を加水分解してビサボロー
ルを製造する従来法を工業的に適用できる製造方法に改
良すべく鋭意研究を重ねた結果、該環化反応を20°C
で測定した誘電率が3.0以下の非極性溶媒の存在下で
行なう場合には、含水率が約30重Ilチまでのギ酸の
使用が可能となり、また反応の制御が容易となシ、しか
も好収率でビサボロールが得られることを見出し、本発
明を完成するに至った。
The present inventors cyclized nerolidol in the presence of formic acid,
Then, as a result of intensive research to improve the conventional method of producing bisabolol by hydrolyzing the product as needed into an industrially applicable production method, the cyclization reaction was carried out at 20°C.
When the reaction is carried out in the presence of a nonpolar solvent with a dielectric constant of 3.0 or less, it is possible to use formic acid with a water content of up to about 30%, and the reaction can be easily controlled. Moreover, they discovered that bisabolol can be obtained in good yield, and have completed the present invention.

本発明で使用する誘電率3.0以下の非極性溶媒として
は、例えばペンタン、ヘキサン、ヘプタン、オクタン、
ノナン、デカン、ヘキサデカン、アイタン、シクロへキ
サン、メチルシクロヘキサン、エチルシクロヘキサン、
シフ京へブタン、シクロオクタンなどの脂環式飽和炭化
水素;ジクロルメトルエン、キシレン、エチルベンゼン
、フロビルベンゼン、ジクロルベンゼンなどの芳香族炭
化水素などが挙げられ、なかでもヘキサン、ヘプタンシ
クロペンタン、シク〜ロヘキサン、エチルシクロヘキサ
ン、ベンゼン、トルエン、キシレンナトが好ましい。こ
れらの溶媒は単独又は2種以上の混合物で用いることが
できる。溶媒の使用量はネロリドールに対して約0.5
〜10倍重量、好ましくは約1〜4倍重量である。
Examples of nonpolar solvents with a dielectric constant of 3.0 or less used in the present invention include pentane, hexane, heptane, octane,
Nonane, decane, hexadecane, itane, cyclohexane, methylcyclohexane, ethylcyclohexane,
Alicyclic saturated hydrocarbons such as Schifkyohebutane and cyclooctane; aromatic hydrocarbons such as dichloromethluene, xylene, ethylbenzene, furobylbenzene, and dichlorobenzene; among them, hexane, heptanecyclopentane, Preferred are cyclohexane, ethylcyclohexane, benzene, toluene, and xylenato. These solvents can be used alone or in a mixture of two or more. The amount of solvent used is approximately 0.5 to nerolidol.
~10 times the weight, preferably about 1 to 4 times the weight.

本発明方法に従うネpリドールの環化反応を約0〜50
°Cの温度範囲で実施すれば、その過度の反応速度が抑
えられ、また脱水反応によるファルネツセン、ビサポレ
ン等の生成が抑制され、好収率でビサボロールのギ酸エ
ステル又はビサボロールのギ酸エステルとビサボロール
との混合物が得られる。また該環化反応を含水率が約5
0重量%までの含水ギ酸の存在下に行なう場合には、そ
の反応速度の低下を差程招くことなく数10分〜数時間
でビサボロールのギ酸エステル又はこれとビサボロール
との混合物を好収率で得ることができる。ギ酸の使用量
はネロリドールに対して約5〜20倍モル量が好ましい
。この環化反応により生成したビサボロールは通常その
大部分がギ酸と反応してエステルに変換する。
The cyclization reaction of nepridol according to the method of the present invention is about 0 to 50
If carried out in the temperature range of °C, the excessive reaction rate can be suppressed, and the production of farnetsene, bisapolene, etc. due to dehydration reaction can be suppressed, and bisabolol formate or bisabolol formate and bisabolol can be combined in good yield. A mixture is obtained. In addition, the cyclization reaction is carried out at a water content of about 5
When carried out in the presence of up to 0% by weight of hydrated formic acid, bisabolol formate or a mixture of bisabolol and bisabolol can be produced in good yield in several tens of minutes to several hours without significantly reducing the reaction rate. Obtainable. The amount of formic acid used is preferably about 5 to 20 times the molar amount of nerolidol. Most of the bisabolol produced by this cyclization reaction is usually converted into an ester by reacting with formic acid.

環化反応後、例えば、反応混合物からビサボロールのギ
酸エステル又はこれとビサボロールとの混合物を含む有
機層を分離し、必要に応じて水で洗滌したのち、この有
機層から溶媒を留去することによシビサボロールのギ酸
エステル又はこれとビサボロールとの混合物の粗生成物
を得ることができる。この粗生成物又は上記の有機層を
次の加水分解反応に付す。
After the cyclization reaction, for example, an organic layer containing bisabolol formate or a mixture of this and bisabolol is separated from the reaction mixture, washed with water as necessary, and then the solvent is distilled off from this organic layer. A crude product of the formate ester of yosibisabolol or a mixture thereof with bisabolol can be obtained. This crude product or the above organic layer is subjected to the next hydrolysis reaction.

環化反応によシ得られたビサボロールのギ酸エステルを
常法に従って加水分解することにょシビサボロールを得
ることができる。この加水分解反応は、例えば水酸化ナ
トリウム、水酸化カリウム、水酸化バリウム、炭酸ナト
リウムなどの塩基性物質の水溶液の存在下、必要に応じ
て環化反応で用いたと同様の溶媒中で、室温ないしは溶
媒の沸点までの温度下に行なう。環化反応に用いたと同
様の溶媒の存在下に加水分解反応を行なう場合には、反
応速度を上げるためにベンジルトリメチルアンモニウム
クロリド、テトラヘンチルアンモニウムクロリド、ラウ
リルトリメチルクロリド、ラウリルジメチルエチルアン
モニウムクルリド、セチルトリメチルアンモニウムプロ
ミド、ベンジルセチルジメチルアンモニウムクロリド、
ステアリルトリメチルアンモニウムクロリド1、ステア
リルジメチルエチルアンモニウムプロミド等の第4級ア
ンモニウム塩;テトラn−ブチルホスホニウムプロミド
、メチルトリn−ブチルホスホニウムプロミド、エチル
トリn−ブチルホスホニウムプロミド、ベンシルトIJ
 n−ブチルホスホニウムクロリド、ラウリルトリn−
ブチルホスホニウムプロミド、セチルトリn−ブチルホ
スホニウムプロミド、ステアリルトリn−ブチルホスホ
ニウムプロミドなどの第4級ホスホニウム塩などの相間
移動触媒をビサボロールのギ酸エステルに対して約0.
01〜10モルチ使用するのが好ましい。反応終了後、
例えば、反応混合物を分液し、ビサボロールを含む有機
層を水洗、乾燥後、必要に応じ、この有機層から溶媒を
留去することによりビサボロールを含む油分を得ること
ができる。この油分から蒸留などの通常一般に用いられ
る分離方法によりビサボロールを分離取得することがで
きる。
Bisabolol can be obtained by hydrolyzing the formic acid ester of bisabolol obtained by the cyclization reaction according to a conventional method. This hydrolysis reaction is carried out at room temperature or in the presence of an aqueous solution of a basic substance such as sodium hydroxide, potassium hydroxide, barium hydroxide, or sodium carbonate, if necessary, in the same solvent used in the cyclization reaction. The reaction is carried out at a temperature up to the boiling point of the solvent. When carrying out the hydrolysis reaction in the presence of the same solvent as used in the cyclization reaction, benzyltrimethylammonium chloride, tetrahentylammonium chloride, lauryltrimethylchloride, lauryldimethylethylammonium chloride, Cetyltrimethylammonium bromide, benzylcetyldimethylammonium chloride,
Quaternary ammonium salts such as stearyltrimethylammonium chloride 1, stearyldimethylethylammonium bromide; tetra n-butylphosphonium bromide, methyltri n-butylphosphonium bromide, ethyltri n-butylphosphonium bromide, benzylt IJ
n-Butylphosphonium chloride, lauryltri n-
A phase transfer catalyst such as a quaternary phosphonium salt such as butylphosphonium bromide, cetyltri n-butylphosphonium bromide, stearyltri n-butylphosphonium bromide, etc. is applied to the formate ester of bisabolol at about 0.0%.
It is preferable to use 0.01 to 10 mol. After the reaction is complete,
For example, the oil containing bisabolol can be obtained by separating the reaction mixture, washing the organic layer containing bisabolol with water, drying, and then distilling off the solvent from this organic layer, if necessary. Bisabolol can be separated and obtained from this oil by a commonly used separation method such as distillation.

以下、実施例によシ本発明を具体的に説明する。Hereinafter, the present invention will be specifically explained using Examples.

実施例1 温度計、冷却器及び攪拌機を付けた1 00 ml容三
ロフラスコにネロリドール11.29.純度80チのギ
酸28.79及びn−ヘキサン19.7gを仕込み、水
浴中で50℃に加温しながら3時間攪拌した。反応終了
後1反応混合液を分液し、上層を等容量の水で2回洗滌
したのち、同一反応装置に仕込み、さらに30%水酸化
ナトリウム水溶液15.54F及びベンジルトリメチル
アンモニウムクロリド0.099を加え、70℃で2時
間攪拌した。
Example 1 Nerolidol 11.29. 28.79 g of formic acid with a purity of 80% and 19.7 g of n-hexane were charged, and the mixture was stirred for 3 hours while being heated to 50° C. in a water bath. After completion of the reaction, one reaction mixture was separated, and the upper layer was washed twice with equal volumes of water, then charged into the same reaction apparatus, and further added with 30% sodium hydroxide aqueous solution 15.54F and benzyltrimethylammonium chloride 0.099%. The mixture was added and stirred at 70°C for 2 hours.

反応終了後、反応混合液を分液し、上層を水洗したのち
、無水硫酸ナトリウムを添加し、−夜放置して乾燥した
。乾燥剤な濾過して得られたp液よりn−へキサ/を留
去し、残留物11.09を得た。
After the reaction was completed, the reaction mixture was separated and the upper layer was washed with water, and anhydrous sodium sulfate was added thereto, followed by drying by leaving overnight. N-hexa/ was distilled off from the p liquid obtained by filtration with a drying agent to obtain a residue of 11.09%.

このものをパラニトロトルエンを内部標準としてGLC
にて分析したところ、ビサボロール5.6g、ファルネ
ソール2.99.ビサボレン1.5g、ファルネツセン
0.49及び未反応のネロリドール0゜11りが含まれ
ていた。ビサボロールの収率は反応したネロリドールを
基準にすると32゜5チであった。
This was analyzed by GLC using para-nitrotoluene as an internal standard.
As a result of analysis, bisabolol 5.6g, farnesol 2.99g. It contained 1.5 g of bisabolene, 0.49 g of farnetsene, and 0.11 g of unreacted nerolidol. The yield of bisabolol was 32.5 cm based on the reacted nerolidol.

比較例1 実施例1におけると同一の反応装置にネロリドール11
.21F及び純度90チのギ酸2.5.5gを仕込み、
室温にて7時間攪拌した。反応終了後、反応混合液を分
液し、上層を等容量の水で2回洗滌したのち、同一反応
装置に仕込み、さら4C30%水酸化ナトリウム水溶液
15..51Fを加え、70°Cで2時間攪拌した。反
応終了後、反応混合液を分液し、下層をジエチルエーテ
/L−20yrtで5回、計60 mlで抽出し、この
エーテル層と上層とを混合したのち、この混合液に無水
硫酸ナトリウムを加え、−夜放置し乾燥した。乾燥剤を
濾過して得られたろ液よりエーテルを留去し、残留物1
1.19を得た。このものを実施例1と同様にしてGL
C分析したところ、ビサボロール2.8g、ファルネソ
ール2.4g、ビサボレン0.95Q、ファルネッセン
0.56Q及び未反応のネロリドール0.35gが含ま
れていた。ビサボロールの収率は反応したネロリドール
を基準にすると25.8%であった。
Comparative Example 1 Nerolidol 11 was added to the same reactor as in Example 1.
.. Prepare 2.5.5g of formic acid with 21F and purity of 90%,
The mixture was stirred at room temperature for 7 hours. After the reaction was completed, the reaction mixture was separated, and the upper layer was washed twice with an equal volume of water, then charged into the same reaction apparatus, and further added with 4C 30% sodium hydroxide aqueous solution 15. .. 51F was added and stirred at 70°C for 2 hours. After the reaction was completed, the reaction mixture was separated, and the lower layer was extracted with diethyl ether/L-20yrt 5 times in a total of 60 ml. After the ether layer and the upper layer were mixed, anhydrous sodium sulfate was added to the mixture. The mixture was added and left overnight to dry. Ether was distilled off from the filtrate obtained by filtering the desiccant, and residue 1
1.19 was obtained. This product was prepared in the same manner as in Example 1 and GL
C analysis revealed that it contained 2.8 g of bisabolol, 2.4 g of farnesol, 0.95 Q of bisabolene, 0.56 Q of farnesene, and 0.35 g of unreacted nerolidol. The yield of bisabolol was 25.8% based on the reacted nerolidol.

実施例2 実施例1におけると同一の反応装置にネロリドール11
.2g、純度98%のギ酸23.51F及びトルエン2
2.49を仕込み、室温で2時間攪拌した。
Example 2 Nerolidol 11 was added to the same reactor as in Example 1.
.. 2g, 98% pure formic acid 23.51F and toluene 2
2.49 was added and stirred at room temperature for 2 hours.

反応終了後、反応混合液を分液し、上層を等容量の水で
2回洗滌したのち、同一反応装置に仕込み、40チ水酸
化ナトリウム水溶液6.7g及びペンジルトリメチルア
ンモニウムクロリド0.099を加え、70℃に加温し
たのち、室温で2時間攪拌した。反応終了後、反応混合
液を分液し、有機層は実施例1と同様な処理を行なった
のち、これよシトルエンを留去して残留物10.8gを
得た。このものを実施例1と同様にしてGLC分析した
ところ、ビサボロール4・27 f、ファルネソール3
.619、ビサポレン0.579、ファルネッセン0.
54g及び未反応のネロリドール1.211Fが含まれ
ていた。ビサボロールの収率は反応したネロリドールを
基準にすると43.2%であった。
After the reaction was completed, the reaction mixture was separated, and the upper layer was washed twice with equal volumes of water, and then charged into the same reactor, and 6.7 g of aqueous sodium 40 thihydroxide solution and 0.099 of penzyltrimethylammonium chloride were added. After the mixture was added and heated to 70°C, the mixture was stirred at room temperature for 2 hours. After the reaction was completed, the reaction mixture was separated into layers, and the organic layer was treated in the same manner as in Example 1, and then citoluene was distilled off to obtain 10.8 g of a residue. When this product was analyzed by GLC in the same manner as in Example 1, bisabolol 4.27f, farnesol 3
.. 619, bisapolene 0.579, farnessen 0.
It contained 54 g and unreacted nerolidol 1.211F. The yield of bisabolol was 43.2% based on the reacted nerolidol.

実施例3 実施例1におけると同一の反応装置にネロリドール11
.2g、純度98%のギ酸25.59及び四塩化炭素5
5.29を仕込み、室温で2時間攪拌した。反応終了後
、反応混合液を分液し、有機層(下層)を等容量の水で
2回洗滌したのち、これよシ四塩化炭素をエバポレータ
ーによシ留去した。
Example 3 Nerolidol 11 was added to the same reactor as in Example 1.
.. 2 g, 98% pure formic acid 25.59 and carbon tetrachloride 5
5.29 and stirred at room temperature for 2 hours. After the reaction was completed, the reaction mixture was separated, and the organic layer (lower layer) was washed twice with an equal volume of water, and then the carbon tetrachloride was distilled off using an evaporator.

この残留物を上記反応装置に50%水酸化ナトリウム水
溶液15.59とともに仕込み、70°Cに加温しなが
ら2時間攪拌した。反応終了後、反応混合液を分液し、
有機層(上層)を水洗したのち、実施例1と同様に乾燥
した。乾燥終了後、この有機層を実施例1と同様にGL
C分析した。ビサボロール4.20g、ファルネソール
3.7Of、ビサボレン1.1Of、ファルネツセン1
.109及び未反応のネロリドール1.229が含まれ
ていた。ビサボロールの収率は反応したネロリドールを
基準にすると42.3%であった。
This residue was charged into the above reaction apparatus along with 15.5 g of a 50% aqueous sodium hydroxide solution, and stirred for 2 hours while heating to 70°C. After the reaction is complete, separate the reaction mixture,
After washing the organic layer (upper layer) with water, it was dried in the same manner as in Example 1. After drying, this organic layer was subjected to GL treatment in the same manner as in Example 1.
C was analyzed. Bisabolol 4.20g, Farnesol 3.7Of, Bisabolene 1.1Of, Farnetsen 1
.. 109 and unreacted nerolidol 1.229. The yield of bisabolol was 42.3% based on the reacted nerolidol.

実施例4 実施例1におけると同一の反応装置にネロリドール11
.2f、純度80チのギ酸28.79及びシクロヘキサ
ンs3qを仕込み、50°Cに加温しながら3時間攪拌
した。反応終了後、反応混合液を分液し、上層を等容量
の水で2回洗滌したのち、同一反応装置に仕込み、さら
に30チ水酸化ナトリウム水溶液15.51F及びベン
ジルトリメチルアンモニウムクロリド0.099を加え
、70℃で2時間攪拌した。反応終了後、反応混合液を
分液し、上層を水洗したのち、無水硫酸ナトリウムを添
加し、−夜装置することによシ乾燥した。乾燥剤をp遇
して得られた炉液よジシクロヘキサンを留去し、その残
留物を実施例1と同様にしてGLC分析シた。ビサボロ
ール4.51f、ファルネソール3.91f、ビサボレ
ン0.659、ファルネツセン0.369及び未反応の
ネロリドール0.539が含まれていた。ビサボロール
の収率は反応したネロリドールを基準にすると41.q
’lrであった。
Example 4 Nerolidol 11 was added to the same reactor as in Example 1.
.. 2f, 28.79 g of formic acid with a purity of 80 g, and 3 q of cyclohexane were added, and the mixture was stirred for 3 hours while heating to 50°C. After the reaction was completed, the reaction mixture was separated, and the upper layer was washed twice with an equal volume of water, then charged into the same reactor, and further added with 15.51F of 30 sodium hydroxide aqueous solution and 0.099 of benzyltrimethylammonium chloride. The mixture was added and stirred at 70°C for 2 hours. After the reaction was completed, the reaction mixture was separated into layers, the upper layer was washed with water, anhydrous sodium sulfate was added thereto, and the mixture was dried by standing overnight. Dicyclohexane was distilled off from the furnace liquid obtained by adding a drying agent, and the residue was analyzed by GLC in the same manner as in Example 1. It contained 4.51f of bisabolol, 3.91f of farnesol, 0.659 of bisabolene, 0.369 of farnetsen, and 0.539 of unreacted nerolidol. The yield of bisabolol is 41% based on the reacted nerolidol. q
It was 'lr.

実施例5 実施例1におけると同一の反応装置にネロリドール11
.21i1.純度98チのギ酸25.59及びスクワラ
ン26gを仕込み、室温で0.5時間攪拌した。反応終
了後1反応混合液を分液し、上層を等容量の水で2回洗
滌したのち、同一反応装置に仕込み、さらに50チ水酸
化ナトリウム水溶液15.59を加え、70°Cに加温
しながら2時間攪拌した。
Example 5 Nerolidol 11 was added to the same reactor as in Example 1.
.. 21i1. 25.59 g of formic acid with a purity of 98% and 26 g of squalane were charged and stirred at room temperature for 0.5 hour. After the reaction was completed, one reaction mixture was separated, and the upper layer was washed twice with an equal volume of water, then charged into the same reactor, and 50% sodium hydroxide aqueous solution (15.59%) was added and heated to 70°C. While stirring, the mixture was stirred for 2 hours.

反応終了後、反応混合液を分液し、上層を水洗したのち
、無水硫酸ナトリウムで乾燥した。乾燥剤を濾過して得
られたp液よシスクワランを留去し、その残留物を実施
例1と同様にGLC分析した。
After the reaction was completed, the reaction mixture was separated, and the upper layer was washed with water and then dried over anhydrous sodium sulfate. Cisqualane was distilled off from the p liquid obtained by filtering the desiccant, and the residue was analyzed by GLC in the same manner as in Example 1.

ビサボロール5.569、ファルネソール2.73g、
ビサボレン0.2f、ファルネツセン0.52g及び未
反応のネロリドール0.259が含まれていた。
Bisabolol 5.569, farnesol 2.73g,
It contained 0.2 f of bisabolene, 0.52 g of farnetusene, and 0.259 unreacted nerolidol.

ビサボロールの収率は反応したネロリドールを基準にす
ると32.1%であった。
The yield of bisabolol was 32.1% based on the reacted nerolidol.

実施例6 実施例1におけると同一の反応装置にネロリドール11
.2g、純度98チのギ酸23.59及びテトラクロル
エチレン21gを仕込み、室温下で5時間攪拌した。反
応終了後、反応混合液を分液し、有機層(下層)を等容
量の水で2回洗滌したのち、テトラクロルエチレンをエ
バポレータにより留去した。この残留物及び50チ水酸
化ナトリウム水溶液15.59を同一反応装置に仕込み
、70°Cに加温しながら2時間攪拌した。反応終了後
、反応混合液を分液し、有機層(上層)を水洗したのち
、実施例1と同様に乾燥した。乾燥終了後、この有機層
を実施例1と同様にGLC分析した。ビサボロール4.
55f、ファルネソール3.45f、ビサボレン0.5
8f、ファルネツセン0.59 Q及rJ未反応のネロ
リドール0.589を含んでいた。ネロリドールの転化
率及び反応したネロリドールを基準にしたビサボロール
の収率はそれぞれ94.8%、58.8チであった。
Example 6 Nerolidol 11 was added to the same reactor as in Example 1.
.. 2 g, 23.59 g of formic acid with a purity of 98%, and 21 g of tetrachloroethylene were charged, and the mixture was stirred at room temperature for 5 hours. After the reaction was completed, the reaction mixture was separated, and the organic layer (lower layer) was washed twice with an equal volume of water, and then tetrachlorethylene was distilled off using an evaporator. This residue and 15.59 g of an aqueous sodium 50 hydroxide solution were charged into the same reactor and stirred for 2 hours while heating to 70°C. After the reaction was completed, the reaction mixture was separated, and the organic layer (upper layer) was washed with water and then dried in the same manner as in Example 1. After drying, this organic layer was analyzed by GLC in the same manner as in Example 1. Bisabolol 4.
55f, farnesol 3.45f, bisabolene 0.5
8f, farnetsen 0.59 Q and rJ unreacted nerolidol 0.589 were contained. The conversion rate of nerolidol and the yield of bisabolol based on the reacted nerolidol were 94.8% and 58.8%, respectively.

比較例2 実施例1におけると同一の反応装置にネロリドール11
.29及び純度85%のギ酸27.099を仕込み、室
温で5時間攪拌した。反応終了後1反応混合液を分液し
、上層を比較例1と同様に処理し、ついで加水分解反応
に付した。得られた反応混合液を比較例1と同様に処理
したのち、GLC分析した。ビサボロール2.749、
ファルネソール2.15f%ビサボレンQ、5j’l、
ファルネツセン0.289及び未反応のネロリドール4
.399が含まれていた。ネロリドールの転化率及び反
応したネロリドールを基準にしたビサボロールの収率は
それぞれ6o、a%、24.7%であった。
Comparative Example 2 Nerolidol 11 was added to the same reactor as in Example 1.
.. 29 and 27.099% of formic acid with a purity of 85% were charged, and the mixture was stirred at room temperature for 5 hours. After the reaction was completed, one reaction mixture was separated, and the upper layer was treated in the same manner as in Comparative Example 1, and then subjected to a hydrolysis reaction. The resulting reaction mixture was treated in the same manner as in Comparative Example 1, and then subjected to GLC analysis. bisabolol 2.749,
Farnesol 2.15f% bisabolene Q, 5j'l,
Farnetsen 0.289 and unreacted nerolidol 4
.. 399 were included. The conversion rate of nerolidol and the yield of bisabolol based on the reacted nerolidol were 6o, a%, and 24.7%, respectively.

比較例3 実施例1におけると同一の反応装置にネロリドール11
.21F及び純度90チのギ酸25.5fを仕込み、5
0°Cに加温しながら1.5時間攪拌した。
Comparative Example 3 Nerolidol 11 was added to the same reactor as in Example 1.
.. Prepare 21F and 25.5f of formic acid with a purity of 90%,
The mixture was stirred for 1.5 hours while warming to 0°C.

反応終了後、反応混合液を分液し、上層を比較例1と同
様に処理し、ついで加水分解反応に付した。
After the reaction was completed, the reaction mixture was separated, and the upper layer was treated in the same manner as in Comparative Example 1, and then subjected to a hydrolysis reaction.

得られた反応混合液を比較例1と同様に処理したのち、
GLC分析した。ビサボロール0.889及びビサボレ
ン5.239が含まれていた。ファルネソール及び未反
応のネロリドールは含まれていなかった。ネロリドール
の転化率及びビサボロールの収率はそれぞれ100チ、
7.85%であった。
After treating the obtained reaction mixture in the same manner as in Comparative Example 1,
GLC analysis was performed. It contained 0.889 bisabolol and 5.239 bisabolene. Farnesol and unreacted nerolidol were not included. The conversion rate of nerolidol and the yield of bisabolol are each 100 Ti,
It was 7.85%.

特許出願人 株式会社り ラ し 代理人 弁理士不予 堅Patent applicant Rishi Co., Ltd. Agent: Patent Attorney Ken Fuyo

Claims (1)

【特許請求の範囲】[Claims] 3.7.11− )リメチルドデカー1.6.10−)
ジエン−5−オールをギ酸の存在下に環化させ、ついで
必要に応じて該生成物を加水分解してビサボロールを製
造するに際し、核環化反応を誘電率5.0以下の非極性
溶媒の存在下に行なうことを特徴とするビサボロールの
製造方法。
3.7.11-) Limethyldodecar 1.6.10-)
When dien-5-ol is cyclized in the presence of formic acid and then optionally hydrolyzed to produce bisabolol, the nuclear cyclization reaction is carried out in a non-polar solvent with a dielectric constant of 5.0 or less. A method for producing bisabolol, characterized by carrying out in the presence of bisabolol.
JP22826583A 1983-12-01 1983-12-01 Production of bisabolol Granted JPS60120828A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22826583A JPS60120828A (en) 1983-12-01 1983-12-01 Production of bisabolol

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22826583A JPS60120828A (en) 1983-12-01 1983-12-01 Production of bisabolol

Publications (2)

Publication Number Publication Date
JPS60120828A true JPS60120828A (en) 1985-06-28
JPS6365052B2 JPS6365052B2 (en) 1988-12-14

Family

ID=16873762

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22826583A Granted JPS60120828A (en) 1983-12-01 1983-12-01 Production of bisabolol

Country Status (1)

Country Link
JP (1) JPS60120828A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7622617B2 (en) 2005-11-07 2009-11-24 Basf Se Method for producing α-bisabolol from farnesol

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7622617B2 (en) 2005-11-07 2009-11-24 Basf Se Method for producing α-bisabolol from farnesol

Also Published As

Publication number Publication date
JPS6365052B2 (en) 1988-12-14

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