JP2008037852A - METHOD FOR PRODUCING omega-BROMO LONG-CHAIN CARBOXYLIC ACID - Google Patents
METHOD FOR PRODUCING omega-BROMO LONG-CHAIN CARBOXYLIC ACID Download PDFInfo
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Abstract
Description
本発明は、ω-ブロモ長鎖カルボン酸の製造法に関する。 The present invention relates to a method for producing an ω-bromo long chain carboxylic acid.
ω-ブロモ長鎖カルボン酸は、化粧品・香粧品分野において、界面活性剤等の製造に有用な原料である。従来、ω-ブロモ長鎖カルボン酸の製造は、例えば、アゼライン酸からKolbe電解、ハーフAg塩化、臭素化して、15−ブロモペンタデカン酸を製造する方法(非特許文献1)、15−メトキシペンタデカン酸にボロントリブロマイドを作用させて15−ブロモペンタデカン酸を製造する方法(非特許文献2)等が報告されている。
しかしながら、これらはいずれも製造に多段階を要するなど問題があり、簡便に製造出来る製法ではなかった。
Omega-bromo long chain carboxylic acid is a useful raw material for the production of surfactants and the like in the cosmetics and cosmetics fields. Conventionally, ω-bromo long chain carboxylic acid is produced by, for example, a method of producing 15-bromopentadecanoic acid from azelaic acid by Kolbe electrolysis, half Ag chlorination and bromination (Non-patent Document 1), 15-methoxypentadecanoic acid. A method for producing 15-bromopentadecanoic acid by allowing boron tribromide to act on (Non-patent Document 2) has been reported.
However, these methods have problems such as requiring a multi-stage production, and are not easy production methods.
また、近年、シクロペンタデカノリド(商品名Pentalide)から、濃硫酸-臭化水素酸を用いて、15−ブロモペンタデカン酸を高収率で得る方法も報告されている(非特許文献3)。
しかしながら、当該方法では、反応系の黒化、不溶物等が生じて水層との分離が難しい、3.5日間の如く長時間還流させる必要がある、等の問題点があり、実製造が困難であった。
However, this method has problems such as blackening of the reaction system, insoluble matter, etc., which makes it difficult to separate from the aqueous layer, and it is necessary to reflux for a long time such as 3.5 days. It was difficult.
本発明は、安価に入手し易い原料を用い、簡易に且つ効率よくω-ブロモ長鎖カルボン酸を得る方法を提供することに関する。 The present invention relates to providing a method for easily and efficiently obtaining a ω-bromo long-chain carboxylic acid using inexpensive and readily available raw materials.
本発明者らは、大環状エステル類を用いたω-ブロモ長鎖カルボン酸の製造法について検討した結果、密閉下で、臭化水素を作用させることにより、副生成物等を生じることなく、定量的に、ω-ハロゲン化長鎖カルボン酸が得られることを見出した。 As a result of studying the production method of ω-bromo long chain carboxylic acid using macrocyclic esters, the present inventors have caused hydrogen bromide to act under sealing without producing a by-product, It was found that ω-halogenated long chain carboxylic acid can be obtained quantitatively.
すなわち、本発明は下記の反応式に示すように、式(1)で表される大環状エステル類と臭化水素とを、酢酸溶媒中、密閉系で反応させることを特徴とする下記式(2)で表されるω-ブロモ長鎖カルボン酸の製造法を提供するものである。 That is, as shown in the following reaction formula, the present invention comprises reacting a macrocyclic ester represented by formula (1) with hydrogen bromide in an acetic acid solvent in a closed system ( The present invention provides a process for producing a ω-bromo long chain carboxylic acid represented by 2).
〔式中、nは12〜16の整数を示す。〕 [In formula, n shows the integer of 12-16. ]
本発明によれば、安価に入手し易い大環状エステル類を用いて、ω-ブロモ長鎖カルボン酸を定量的に製造することができる。また、本発明の方法は、短時間で行うことができ、反応系が黒化したり、不溶物や副生成物を生じることなく、後処理も容易である。従って、界面活性剤等の製造原料であるω-ブロモ長鎖カルボン酸の工業的製造法として有用である。 According to the present invention, ω-bromo long chain carboxylic acid can be quantitatively produced using macrocyclic esters that are easily available at low cost. Further, the method of the present invention can be carried out in a short time, and the post-treatment is easy without blackening the reaction system or generating insoluble matter or by-products. Therefore, it is useful as an industrial production method of ω-bromo long chain carboxylic acid which is a raw material for producing a surfactant and the like.
本発明において、一般式(1)及び(2)中の、nは12〜16の整数を示すが、このうち、15又は16が好ましい。 In the present invention, n in the general formulas (1) and (2) represents an integer of 12 to 16, of which 15 or 16 is preferable.
本発明の反応は、酢酸の存在下に行われ、酢酸を溶媒として行うことができる。前述の非特許文献2に開示されているように、濃硫酸−臭化水素酸の系を用い、例えばペンタリドを反応させた場合、目的物である15−ブロモペンタデカン酸との分離が困難な15−(15−ブロモペンタデシルオキシ)ペンタデカン酸が副生し、高純度の15−ブロモペンタデカン酸を得ることは困難となる。
ここで、酢酸の使用量は、大環状エステル類に対して、0.1〜10倍量、好適には1〜5倍量である。
尚、反応溶媒として、トルエン、ヘキサン、キシレン等の非水系の溶媒を酢酸と共に用いることも可能であるが、酢酸のみを溶媒とするのが特に好ましい。
The reaction of the present invention is carried out in the presence of acetic acid, and acetic acid can be used as a solvent. As disclosed in Non-Patent Document 2 described above, when a concentrated sulfuric acid-hydrobromic acid system is used and, for example, pentalide is reacted, it is difficult to separate from the target 15-bromopentadecanoic acid 15 -(15-Bromopentadecyloxy) pentadecanoic acid is by-produced and it is difficult to obtain high-purity 15-bromopentadecanoic acid.
Here, the usage-amount of acetic acid is 0.1-10 times amount with respect to macrocyclic esters, Preferably it is 1-5 times amount.
As a reaction solvent, a non-aqueous solvent such as toluene, hexane or xylene can be used together with acetic acid, but it is particularly preferable to use only acetic acid as a solvent.
臭化水素の使用量は、大環状エステル類1モルに対して1〜3倍モル用いるのが好ましく、1.0〜2.0倍モルの使用が更に好ましい。 As for the usage-amount of hydrogen bromide, it is preferable to use 1-3 times mole with respect to 1 mol of macrocyclic esters, and use of 1.0-2.0 times mole is still more preferable.
本発明の反応は、密閉系で行われる。密閉系で反応を行うことにより、臭化水素の損失を防ぐことができ、反応が効率的に進行すると考えられるが、開放系では、冷却管を備えた装置を用いて、本反応を行った場合、臭化水素を過剰に使用しても、目的物の収率は50%程度に止まる(比較例参照)。
本発明の製造法に用いられる密閉系の反応装置としては、オートクレーブ等の耐熱耐圧装置であれば良く、内部に攪拌装置を有しているものが好ましい。
The reaction of the present invention is carried out in a closed system. By conducting the reaction in a closed system, loss of hydrogen bromide can be prevented and the reaction is considered to proceed efficiently. However, in an open system, this reaction was performed using a device equipped with a cooling pipe. In this case, even if hydrogen bromide is used in excess, the yield of the target product is only about 50% (see Comparative Example).
The closed reactor used in the production method of the present invention may be a heat and pressure resistant device such as an autoclave, and preferably has a stirring device inside.
反応温度は、10℃〜150℃が好ましく、50℃〜130℃の範囲が特に好ましい。
反応時間は、1〜30時間が好ましく、5〜20時間がより好ましい。
The reaction temperature is preferably 10 ° C to 150 ° C, particularly preferably in the range of 50 ° C to 130 ° C.
The reaction time is preferably 1 to 30 hours, more preferably 5 to 20 hours.
斯くして得られるω-ブロモ長鎖カルボン酸は、必要に応じて、有機合成化学で常用される精製法、例えば濾過、洗浄、乾燥、再結晶、各種クロマトグラフィー等により精製し、単離することができる。 The ω-bromo long chain carboxylic acid thus obtained is purified and isolated, if necessary, by a purification method commonly used in organic synthetic chemistry, for example, filtration, washing, drying, recrystallization, various chromatography, etc. be able to.
以下に反応の詳細について実施例を用いて説明する。
尚、本反応の生成物は、文献既知の手法により、別途合成した標品と、ガスクロマトグラフィー及び1H-NMRを比較し、確認した。
The details of the reaction will be described below using examples.
The product of this reaction was confirmed by comparing a separately synthesized sample with gas chromatography and 1 H-NMR by a method known in the literature.
実施例1 15-ブロモペンタデカン酸の合成(1)
シクロペンタデカノリド14.3g(59.5mmol)、32%臭化水素/酢酸溶液24.8g(98.0mmol、1.6eq)を、テフロン(登録商標)で保護された100mlオートクレーブに入れ、窒素置換した後、密閉し、120℃のオイルバスにつけて、16時間、攪拌した。攪拌には、マグネチックスターラーを使用した。冷却後、水14mlを加え、酢酸エチル200mlを用い、分液ロートに移送した。この酢酸エチル層を、キャピラリーGCにて分析した結果、原料は消失し、目的物15-ブロモペンタデカン酸のみのピークが観測された。飽和食塩水で洗浄後、硫酸マグネシウムで乾燥し、ろ過、減圧濃縮後、酢酸エチル-n-ヘキサン混合溶媒で晶析、目的物17.1g(収率90%)を得た。
Example 1 Synthesis of 15-bromopentadecanoic acid (1)
14.3 g (59.5 mmol) of cyclopentadecanolide and 24.8 g (98.0 mmol, 1.6 eq) of a 32% hydrogen bromide / acetic acid solution were placed in a 100 ml autoclave protected with Teflon. After substituting with nitrogen, it was sealed, placed in an oil bath at 120 ° C., and stirred for 16 hours. A magnetic stirrer was used for stirring. After cooling, 14 ml of water was added and transferred to a separatory funnel using 200 ml of ethyl acetate. As a result of analyzing this ethyl acetate layer with capillary GC, the raw material disappeared and a peak of only the target product 15-bromopentadecanoic acid was observed. The extract was washed with saturated brine, dried over magnesium sulfate, filtered, concentrated under reduced pressure, and crystallized from a mixed solvent of ethyl acetate-n-hexane to obtain 17.1 g (yield 90%) of the desired product.
実施例2 15-ブロモペンタデカン酸の合成(2)
シクロペンタデカノリド14.3g(59.5mmol)、32%臭化水素/酢酸溶液24.8g(98.0mmol、1.6eq)を、テフロン(登録商標)で保護された100mlオートクレーブに入れ、窒素置換した後、密閉し、60℃のオイルバスにつけて、16時間、攪拌した。攪拌には、マグネチックスターラーを使用した。冷却後、水14mlを加え、熱ヘキサン200mlを用い、分液ロートに移送した。イオン交換水で洗浄後、硫酸マグネシウムで乾燥し、ろ過、n-ヘキサンで晶析することで、目的物17.4g(収率91%)を得た。
Example 2 Synthesis of 15-bromopentadecanoic acid (2)
14.3 g (59.5 mmol) of cyclopentadecanolide and 24.8 g (98.0 mmol, 1.6 eq) of a 32% hydrogen bromide / acetic acid solution were placed in a 100 ml autoclave protected with Teflon. After substituting with nitrogen, it was sealed, placed in an oil bath at 60 ° C., and stirred for 16 hours. A magnetic stirrer was used for stirring. After cooling, 14 ml of water was added and transferred to a separatory funnel using 200 ml of hot hexane. After washing with ion-exchanged water, drying with magnesium sulfate, filtration and crystallization with n-hexane gave 17.4 g (yield 91%) of the desired product.
比較例 15-ブロモペンタデカン酸の合成(開放系)
シクロペンタデカノリド1.0g(4.2mmol)、32%臭化水素/酢酸溶液3.3g(13.1mmol、3.1eq)を、還流冷却管、マグネチックスターラーを備えた50ml2口フラスコに入れ、60℃のオイルバスにつけて、窒素雰囲気下、16時間、攪拌した。サンプリングし、GC分析した結果、面積百分率は、目的物15-ブロモペンタデカン酸10%、原料シクロペンタデカノリド89%、副生物15-アセトキシペンタデカン酸1%であった。更に、80℃のオイルバスにて、8時間加熱、攪拌した結果、その面積百分率は、目的物31%、原料65%、副生物4%。更に、100℃のオイルバスにて、20時間加熱、攪拌した結果、その面積百分率は、目的物42%、原料52%、副生物6%。32%臭化水素/酢酸溶液3g(11.9mmol、2.8eq)を追加したのち、100℃のオイルバスにて、2時間加熱、攪拌した結果、その面積百分率は、目的物47%、原料47%、副生物6%であった。
Comparative Example 15 Synthesis of bromopentadecanoic acid (open system)
1.0 g (4.2 mmol) of cyclopentadecanolide and 3.3 g (13.1 mmol, 3.1 eq) of a 32% hydrogen bromide / acetic acid solution were placed in a 50 ml two-necked flask equipped with a reflux condenser and a magnetic stirrer. The mixture was placed in a 60 ° C. oil bath and stirred for 16 hours under a nitrogen atmosphere. As a result of sampling and GC analysis, the area percentage was 10% of the target product 15-bromopentadecanoic acid, 89% of raw material cyclopentadecanolide, and 1% of by-product 15-acetoxypentadecanoic acid. Furthermore, as a result of heating and stirring in an oil bath at 80 ° C. for 8 hours, the area percentage was 31% of the target product, 65% of the raw material, and 4% of the by-product. Furthermore, as a result of heating and stirring in an oil bath at 100 ° C. for 20 hours, the area percentage was 42% for the target product, 52% for the raw material, and 6% for the by-product. After adding 3 g (11.9 mmol, 2.8 eq) of 32% hydrogen bromide / acetic acid solution and heating and stirring in an oil bath at 100 ° C. for 2 hours, the area percentage was 47% of the target product, 47% and 6% by-product.
Claims (2)
で表される大環状エステル類と臭化水素とを、酢酸溶媒中、密閉系で反応させることを特徴とする下記式(2)
で表されるω-ブロモ長鎖カルボン酸の製造法。 Following formula (1)
Wherein the macrocyclic ester represented by formula (2) is reacted with hydrogen bromide in an acetic acid solvent in a closed system (2)
The manufacturing method of the omega-bromo long-chain carboxylic acid represented by these.
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008129753A1 (en) * | 2007-04-04 | 2008-10-30 | Kao Corporation | Method for producing cross-coupling compound |
JP2009149546A (en) * | 2007-12-19 | 2009-07-09 | Kao Corp | Method for producing branched fatty acid |
CN115028528A (en) * | 2022-08-04 | 2022-09-09 | 东莞理工学院 | Method for synthesizing 4-bromovaleric acid from gamma-valerolactone |
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JPS4935326A (en) * | 1972-08-01 | 1974-04-01 | ||
JPH05155805A (en) * | 1991-12-05 | 1993-06-22 | Kao Corp | Production of halogenated carboxylic acid |
US20030232820A1 (en) * | 2001-08-29 | 2003-12-18 | Saul Wolfe | Method for synthesizing oxazinones |
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Publication number | Priority date | Publication date | Assignee | Title |
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JPS4935326A (en) * | 1972-08-01 | 1974-04-01 | ||
JPH05155805A (en) * | 1991-12-05 | 1993-06-22 | Kao Corp | Production of halogenated carboxylic acid |
US20030232820A1 (en) * | 2001-08-29 | 2003-12-18 | Saul Wolfe | Method for synthesizing oxazinones |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008129753A1 (en) * | 2007-04-04 | 2008-10-30 | Kao Corporation | Method for producing cross-coupling compound |
US8283482B2 (en) | 2007-04-04 | 2012-10-09 | Kao Corporation | Method for producing cross-coupling compound |
JP2009149546A (en) * | 2007-12-19 | 2009-07-09 | Kao Corp | Method for producing branched fatty acid |
CN115028528A (en) * | 2022-08-04 | 2022-09-09 | 东莞理工学院 | Method for synthesizing 4-bromovaleric acid from gamma-valerolactone |
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