JP4143163B2 - Method for producing amide derivative - Google Patents
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- JP4143163B2 JP4143163B2 JP10921198A JP10921198A JP4143163B2 JP 4143163 B2 JP4143163 B2 JP 4143163B2 JP 10921198 A JP10921198 A JP 10921198A JP 10921198 A JP10921198 A JP 10921198A JP 4143163 B2 JP4143163 B2 JP 4143163B2
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Description
【0001】
【発明の属する技術分野】
本発明は、アミノカルボン酸又は環状ラクタムとジカルボン酸ジハライドを出発原料とするビスアミドカルボン酸エステルの製造法に関する。
【0002】
【従来の技術及び発明が解決しようとする課題】
従来、ビスアミドカルボン酸エステルは、種々の有用な化合物の製造における原料として用いられている。これらの製造法としては、アミノカルボン酸を出発原料とする方法が用いられており、具体的には、(1)アミノカルボン酸を水酸化ナトリウム等の存在下、水又は水−アルコールの溶媒中で、ジカルボン酸ジハライドによりアシル化し(ショッテンバウマン法)、そのあとエステル化する方法、(2)アミノカルボン酸を一旦酸触媒でエステル化した後、酸触媒を中和して遊離のアミノカルボン酸エステルを取り出し、ジカルボン酸ジハライドによりアシル化を行う方法(Polymer Bulletin, 8, 109-116(1982))が用いられている。
【0003】
しかし上記(1)の製造法は、アミノ酸等の高水溶性のアミノカルボン酸を用いた製造法としては有用であるものの、炭素数が多いω−アミノアルキルカルボン酸等の低水溶性のアミノカルボン酸を用いた製造法としては、アミノカルボン酸を溶解させるのに大量の反応溶媒を必要としたり生成物が反応系中に析出するという性質を有しているため、操作が煩雑になるという問題点を有している。また、上記(2)の製造法は、生成する遊離のアミノカルボン酸エステルが極めて重合しやすいという性質を有するため、高収率が望めないという問題点を有している。このように、ビスアミドカルボン酸エステルを工業的に安価で簡便に製造する方法は、いまだ知られていなかった。
【0004】
従って、本発明は、アミノカルボン酸等から工業的に安価で簡便にアミド誘導体を製造する方法を提供することを目的とする。
【0005】
【課題を解決するための手段】
本発明者らは、アミノカルボン酸又は環状ラクタムを特定の酸触媒の存在下特定のアルコールでエステル化した後、そのまま過剰のアルコールを留去し、続いてジカルボン酸ジハライドを用いてアシル化反応を行うことにより、大量の反応溶媒を必要としたり、中間生成物が重合する等の問題がなく、さらに中間生成物が液状で得られることから製造工程が複雑になるという問題もないため、アミド化合物を安価かつ容易に製造できることを見出し、本発明を完成した。
【0006】
本発明方法は、次の反応工程式で表すことができる。
【0007】
【化4】
【0008】
〔式中、R1 及びR2 は同一又は異なって水素原子又は炭素数1〜6の直鎖アルキル基を示し、R3 は炭素数2以上の一価アルコール由来の基を示し、COR4COはジカルボン酸ジハライド由来の基を示し、Xはハロゲン原子を示し、nは1〜16の数を示す〕
【0009】
すなわち、本発明は一般式(1)で表されるアミノカルボン酸又は一般式(2)で表される環状ラクタムに、無機酸の存在下、炭素数2以上の一価アルコールを反応させ、未反応のアルコールを留去し、続いて三級アミンの存在下にジカルボン酸ジハライドを反応させることを特徴とする一般式(3)で表されるアミド誘導体の製造法を提供するものである。
【0010】
【発明の実施の形態】
以下、各工程毎に本発明を説明する。
【0011】
(工程1)
本工程は、アミノカルボン酸(1)又は、環状ラクタム(2)に、無機酸の存在下、R3OHで表される一価アルコールを反応せしめる工程である。
【0012】
式(1)又は式(2)中、R1 又はR2 としては、所望のアミド誘導体(3)に対応するものを用いればよいが、反応性及び収率の点からR1 、R2 は水素原子、メチル基、エチル基が好ましい。また、n個のR1 及びR2 は同一又は異なっていてもよい。
【0013】
また、nは1〜16であり、所望のアミド誘導体(3)に対応する値のものを用いればよいが、反応性及び収率の点から、2〜12が好ましく、5〜12が特に好ましい。
【0014】
本発明製造法で用いられるアミノカルボン酸(1)の好ましい具体例としては、6−アミノヘキサン酸、11−アミノウンデカン酸、12−アミノドデカン酸等が挙げられる。
【0015】
また、本発明製造法で用いられる環状ラクタム(2)の好ましい具体例としては、ε−カプロラクタム、ウンデカラクタム、ラウリンラクタム等が挙げられる。
【0016】
R3OHは、炭素数2以上の一価アルコールを示し、好ましいR3 は炭素数2〜40までの直鎖、分岐鎖又は環状のアルキル基である。本発明においては、かかるアルコールは上記範囲内のものであれば、所望のアミド誘導体(3)に対応するものを用いればよいが、得られるアミノカルボン酸エステルが液状又は溶媒にとけやすくなる点、反応性、収率及び反応終了後の除去のしやすさの点から炭素数2〜12の直鎖、分岐鎖又は環状のアルコールを用いるのが好ましく、炭素数2〜8の直鎖、分岐鎖又は環状のアルコールを用いるのがさらに好ましく、エタノール、n−プロパノール、i−プロパノール、i−ブタノール、2−エチルヘキサノールが特に好ましく、エタノール、i−ブタノールが最も好ましい。
【0017】
また、ここで用いられる無機酸としては、特に制限はないが、特に二価又は三価の無機酸が好ましい。具体的には、硫酸、リン酸が挙げられ、中でも生成するアミノカルボン酸エステルを溶液状又は液状に保つことができることから硫酸が好ましい。
【0018】
反応は無溶媒下で行ってもよく、また不活性溶媒中で行ってもよい。
ここで用いられる不活性溶媒としては、ヘキサン等の炭化水素系溶媒;ベンゼン、トルエン、キシレン等の芳香族系溶媒;ジエチルエーテル、テトラヒドロフラン等のエーテル系溶媒等が挙げられる。
【0019】
この工程は、反応液を常圧下又は減圧下、必要に応じて加熱や脱水することにより行われる。ここで反応温度としては室温〜200℃、好ましくは50℃〜その気圧下における用いた一価アルコールの沸点の範囲である。
【0020】
(工程2)
この工程は、工程1で得られた反応液中の過剰のアルコールを留去する工程である。かかる留去は常圧下又は減圧下、必要に応じて加熱下又は冷却下で行われる。ここで反応温度としては0〜200℃、好ましくは20℃〜その気圧下における用いた一価アルコールの沸点の範囲である。
【0021】
(工程3)
この反応は、工程2で得られた反応液を無溶媒又は不活性溶媒中、三級アミンの存在下、ジカルボン酸ジハライド(XCOR4COX)と反応せしめる工程である。
【0022】
ここで用いられるジカルボン酸ジハライドにおいて、R4 は好ましくは炭素数1〜40の二価の炭化水素基を示し、さらに好ましくは炭素数1〜22の直鎖、分岐鎖又は環状の二価の炭化水素基を示し、特に好ましくは炭素数1〜22の直鎖又は分岐鎖のアルキレン基を示す。また、Xは塩素、臭素、ヨウ素等のハロゲン原子を示す。かかるジカルボン酸ジハライドの具体例としては、マロン酸ジクロリド、コハク酸ジクロリド、グルタル酸ジクロリド、アジピン酸ジクロリド、ピメリン酸ジクロリド、スベリン酸ジクロリド、アゼライン酸ジクロリド、セバシン酸ジクロリド、ドデカンジカルボン酸ジクロリド、1,18−オクタデカンジカルボン酸ジクロリド、エイコサンジカルボン酸ジクロリド、2−メチルコハク酸ジクロリド、2,2−ジメチルコハク酸ジクロリド、3,3−ジエチルグルタル酸ジクロリド、ヘキサヒドロフタル酸ジクロリド、フタル酸ジクロリド、マレイン酸ジクロリド、アセチレンジカルボン酸ジクロリド、フタル酸ジクロリド等が挙げられる。
【0023】
ここで用いられる不活性溶媒としては、ヘキサン、トルエン、キシレン、ベンゼン、ジエチルエーテル、テトラヒドロフラン、塩化メチレン、クロロホルム等が挙げられる。
【0024】
ここで用いられる三級アミンとしては、トリメチルアミン、トリエチルアミン、トリプロピルアミン、トリブチルアミン、ピリジン、ジメチルピリジン等が挙げられる。
【0025】
この工程は、0〜200℃の範囲内で行われ、10〜100℃の範囲内で行うのが好ましい。
【0026】
反応終了後、反応混合物から生成した三級アミン塩を水洗等により除去し、溶媒を留去すれば、容易に目的のアミド誘導体が得られる。
【0027】
【発明の効果】
本発明のアミド誘導体の製造法は、中間に生成するアミノカルボン酸エステル塩が液状又は溶媒に溶けやすいため、固体化合物を経由せず、工業的に極めて製造が容易で、アシル化工程全体が工業的に有利な方法である。
【0028】
【実施例】
次に実施例を挙げて本発明を詳細に説明するが、本発明はこれに何ら限定されるものではない。
【0029】
実施例1
R1 〜R4 及びnが次に示すものであるアミド誘導体(3−a)の製造:
【0030】
【化5】
【0031】
12−アミノドデカン酸100gを1リットルフラスコに仕込み、イソブタノール344gを加えて攪拌を開始した。次いで、50℃に加熱して、硫酸50gを滴下した。滴下終了後加熱還流させ、5時間後70℃に冷却し、未反応のイソブタノールを減圧留去すると液状の化合物が得られた。これにトルエン260gを加えて溶解させた。次いで、50℃にてトリエチルアミン155gを10分かけて滴下した。これに、50℃にてセバシン酸ジクロリド56gを1時間かけて滴下し、さらに70℃で3時間反応させた。反応終了後、生成した塩を水洗により除去し、溶媒を減圧留去して標記化合物(3−a)319gを得た。
【0032】
実施例2
R1 〜R4 及びnが次に示すものであるアミド誘導体(3−b)の製造:
【0033】
【化6】
【0034】
実施例1において、イソブタノールの代りにエタノールを、またセバシン酸56gの代りにアジピン酸ジクロリド43gを1時間かけて滴下し、さらに60℃で2時間反応させた以外は実施例1と同様にして、標記化合物(3−b)265gを得た。
【0035】
実施例3
R1 〜R4 及びnが次に示すものであるアミド誘導体(3−c)の製造:
【0036】
【化7】
【0037】
ε−カプロラクタム113gを2リットルフラスコに仕込み、イソブタノール741gを加えて攪拌を開始した。次いで、50℃に加熱して、硫酸108gを滴下した。滴下終了後加熱還流させ、22時間後70℃に冷却し、未反応のイソブタノールを減圧留去すると液状の化合物が得られた。これにトルエン250gを加えて溶解させた。次いで、50℃にてトリエチルアミン334gを30分かけて滴下した。これに、50℃にてセバシン酸ジクロリド120gを1時間かけて滴下し、さらに70℃で5時間反応させた。反応終了後、生成した塩を水洗により除去し、溶媒を減圧留去して標記化合物(3−c)509gを得た。[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a process for producing a bisamide carboxylic acid ester using aminocarboxylic acid or cyclic lactam and dicarboxylic acid dihalide as starting materials.
[0002]
[Prior art and problems to be solved by the invention]
Conventionally, bisamide carboxylic acid esters have been used as raw materials in the production of various useful compounds. As these production methods, a method using an aminocarboxylic acid as a starting material is used. Specifically, (1) the aminocarboxylic acid in the presence of sodium hydroxide or the like in water or a water-alcohol solvent. In the method of acylating with dicarboxylic acid dihalide (Schotten-Baumann method) and then esterifying, (2) once esterifying aminocarboxylic acid with acid catalyst, neutralizing acid catalyst and free aminocarboxylic acid A method (Polymer Bulletin, 8, 109-116 (1982)) in which an ester is taken out and acylated with dicarboxylic acid dihalide is used.
[0003]
However, although the production method (1) is useful as a production method using a highly water-soluble aminocarboxylic acid such as an amino acid, it has a low water-soluble aminocarboxylic acid such as an ω-aminoalkylcarboxylic acid having a large number of carbon atoms. As a production method using an acid, there is a problem that a large amount of a reaction solvent is required to dissolve an aminocarboxylic acid or the product is precipitated in the reaction system, which makes the operation complicated. Has a point. In addition, the production method (2) has a problem that a high yield cannot be expected because the produced free aminocarboxylic acid ester has a property of being extremely easily polymerized. Thus, the method of manufacturing bisamide carboxylic acid ester industrially cheaply and simply has not been known yet.
[0004]
Accordingly, an object of the present invention is to provide a method for easily and conveniently producing an amide derivative from an aminocarboxylic acid or the like on an industrial scale.
[0005]
[Means for Solving the Problems]
The present inventors esterify an aminocarboxylic acid or a cyclic lactam with a specific alcohol in the presence of a specific acid catalyst, and then distill off excess alcohol as it is, followed by an acylation reaction using dicarboxylic acid dihalide. By doing so, there is no problem that a large amount of reaction solvent is required or the intermediate product is polymerized, and there is no problem that the production process is complicated because the intermediate product is obtained in liquid form. Was found to be inexpensive and easy to produce, and the present invention was completed.
[0006]
The method of the present invention can be represented by the following reaction process formula.
[0007]
[Formula 4]
[0008]
[Wherein, R 1 and R 2 are the same or different and represent a hydrogen atom or a linear alkyl group having 1 to 6 carbon atoms, R 3 represents a group derived from a monohydric alcohol having 2 or more carbon atoms, COR 4 CO Represents a group derived from dicarboxylic acid dihalide, X represents a halogen atom, and n represents a number of 1 to 16.
[0009]
That is, in the present invention, an aminocarboxylic acid represented by the general formula (1) or a cyclic lactam represented by the general formula (2) is reacted with a monohydric alcohol having 2 or more carbon atoms in the presence of an inorganic acid. The present invention provides a method for producing an amide derivative represented by the general formula (3), wherein the alcohol in the reaction is distilled off, followed by reaction with a dicarboxylic acid dihalide in the presence of a tertiary amine.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the present invention will be described for each step.
[0011]
(Process 1)
This step is a step of reacting the monocarboxylic alcohol represented by R 3 OH with the aminocarboxylic acid (1) or the cyclic lactam (2) in the presence of an inorganic acid.
[0012]
In formula (1) or formula (2), as R 1 or R 2 , those corresponding to the desired amide derivative (3) may be used. From the viewpoint of reactivity and yield, R 1 and R 2 are A hydrogen atom, a methyl group, and an ethyl group are preferable. Further, n R 1 and R 2 may be the same or different.
[0013]
Moreover, n is 1-16, What is necessary is just to use the thing of the value corresponding to a desired amide derivative (3), but 2-12 are preferable from the point of reactivity and a yield, and 5-12 are especially preferable. .
[0014]
Preferable specific examples of aminocarboxylic acid (1) used in the production method of the present invention include 6-aminohexanoic acid, 11-aminoundecanoic acid, 12-aminododecanoic acid and the like.
[0015]
Further, preferred specific examples of the cyclic lactam (2) used in the production method of the present invention include ε-caprolactam, undecalactam, laurin lactam and the like.
[0016]
R 3 OH represents a monohydric alcohol having 2 or more carbon atoms, and preferred R 3 is a linear, branched or cyclic alkyl group having 2 to 40 carbon atoms. In the present invention, as long as the alcohol is within the above range, the alcohol corresponding to the desired amide derivative (3) may be used, but the obtained aminocarboxylic acid ester is easily dissolved in a liquid or solvent, From the viewpoint of reactivity, yield, and ease of removal after completion of the reaction, it is preferable to use a linear, branched or cyclic alcohol having 2 to 12 carbon atoms, and a linear or branched chain having 2 to 8 carbon atoms. Alternatively, it is more preferable to use a cyclic alcohol, ethanol, n-propanol, i-propanol, i-butanol and 2-ethylhexanol are particularly preferable, and ethanol and i-butanol are most preferable.
[0017]
In addition, the inorganic acid used here is not particularly limited, but a divalent or trivalent inorganic acid is particularly preferable. Specific examples include sulfuric acid and phosphoric acid, and sulfuric acid is preferred because the aminocarboxylic acid ester produced can be kept in solution or in liquid form.
[0018]
The reaction may be performed in the absence of a solvent or in an inert solvent.
Examples of the inert solvent used here include hydrocarbon solvents such as hexane; aromatic solvents such as benzene, toluene and xylene; ether solvents such as diethyl ether and tetrahydrofuran.
[0019]
This step is performed by heating or dehydrating the reaction solution under normal pressure or reduced pressure as necessary. Here, the reaction temperature ranges from room temperature to 200 ° C., preferably from 50 ° C. to the boiling point of the monohydric alcohol used under the atmospheric pressure.
[0020]
(Process 2)
This step is a step of distilling off excess alcohol in the reaction solution obtained in step 1. Such distillation is carried out under normal pressure or reduced pressure and, if necessary, under heating or cooling. Here, the reaction temperature ranges from 0 to 200 ° C., preferably from 20 ° C. to the boiling point of the monohydric alcohol used under the atmospheric pressure.
[0021]
(Process 3)
This reaction is a step of reacting the reaction solution obtained in Step 2 with dicarboxylic acid dihalide (XCOR 4 COX) in the presence of a tertiary amine in a solvent-free or inert solvent.
[0022]
In the dicarboxylic acid dihalide used here, R 4 preferably represents a divalent hydrocarbon group having 1 to 40 carbon atoms, more preferably a linear, branched or cyclic divalent carbon group having 1 to 22 carbon atoms. A hydrogen group is particularly preferable, and a linear or branched alkylene group having 1 to 22 carbon atoms is particularly preferable. X represents a halogen atom such as chlorine, bromine or iodine. Specific examples of such dicarboxylic acid dihalides include malonic acid dichloride, succinic acid dichloride, glutaric acid dichloride, adipic acid dichloride, pimelic acid dichloride, suberic acid dichloride, azelaic acid dichloride, sebacic acid dichloride, dodecanedicarboxylic acid dichloride, 1,18. -Octadecanedicarboxylic acid dichloride, eicosanedicarboxylic acid dichloride, 2-methylsuccinic acid dichloride, 2,2-dimethylsuccinic acid dichloride, 3,3-diethylglutaric acid dichloride, hexahydrophthalic acid dichloride, phthalic acid dichloride, maleic acid dichloride, Acetylenedicarboxylic acid dichloride, phthalic acid dichloride and the like can be mentioned.
[0023]
Examples of the inert solvent used here include hexane, toluene, xylene, benzene, diethyl ether, tetrahydrofuran, methylene chloride, chloroform and the like.
[0024]
Examples of the tertiary amine used here include trimethylamine, triethylamine, tripropylamine, tributylamine, pyridine, dimethylpyridine, and the like.
[0025]
This step is performed within a range of 0 to 200 ° C, and preferably performed within a range of 10 to 100 ° C.
[0026]
After completion of the reaction, the tertiary amide salt produced from the reaction mixture is removed by washing with water and the solvent is distilled off to easily obtain the desired amide derivative.
[0027]
【The invention's effect】
In the method for producing the amide derivative of the present invention, since the aminocarboxylic acid ester salt formed in the middle is easily dissolved in a liquid or solvent, it is extremely easy to produce industrially without passing through a solid compound, and the entire acylation process is industrial. This is an advantageous method.
[0028]
【Example】
EXAMPLES Next, although an Example is given and this invention is demonstrated in detail, this invention is not limited to this at all.
[0029]
Example 1
Production of amide derivative (3-a) wherein R 1 to R 4 and n are as follows:
[0030]
[Chemical formula 5]
[0031]
100 g of 12-aminododecanoic acid was charged into a 1 liter flask, and 344 g of isobutanol was added to start stirring. Subsequently, it heated at 50 degreeC and 50 g of sulfuric acid was dripped. After completion of dropping, the mixture was heated to reflux, and after 5 hours, cooled to 70 ° C., and unreacted isobutanol was distilled off under reduced pressure to obtain a liquid compound. To this, 260 g of toluene was added and dissolved. Next, 155 g of triethylamine was added dropwise at 50 ° C. over 10 minutes. To this, 56 g of sebacic acid dichloride was added dropwise at 50 ° C. over 1 hour, and further reacted at 70 ° C. for 3 hours. After completion of the reaction, the produced salt was removed by washing with water, and the solvent was distilled off under reduced pressure to obtain 319 g of the title compound (3-a).
[0032]
Example 2
Production of amide derivative (3-b) in which R 1 to R 4 and n are as follows:
[0033]
[Chemical 6]
[0034]
In Example 1, ethanol was used instead of isobutanol, and 43 g of adipic acid dichloride was added dropwise over 1 hour instead of 56 g of sebacic acid, and the reaction was further continued at 60 ° C. for 2 hours. To 265 g of the title compound (3-b).
[0035]
Example 3
Production of amide derivative (3-c) wherein R 1 to R 4 and n are as follows:
[0036]
[Chemical 7]
[0037]
113 g of ε-caprolactam was charged into a 2 liter flask, and 741 g of isobutanol was added to start stirring. Subsequently, it heated at 50 degreeC and 108 g of sulfuric acid was dripped. After completion of the dropwise addition, the mixture was heated to reflux, then cooled to 70 ° C. after 22 hours, and unreacted isobutanol was distilled off under reduced pressure to obtain a liquid compound. To this, 250 g of toluene was added and dissolved. Next, 334 g of triethylamine was added dropwise at 50 ° C. over 30 minutes. To this, 120 g of sebacic acid dichloride was added dropwise at 50 ° C. over 1 hour, and further reacted at 70 ° C. for 5 hours. After completion of the reaction, the produced salt was removed by washing with water, and the solvent was distilled off under reduced pressure to obtain 509 g of the title compound (3-c).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10921198A JP4143163B2 (en) | 1998-04-20 | 1998-04-20 | Method for producing amide derivative |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10921198A JP4143163B2 (en) | 1998-04-20 | 1998-04-20 | Method for producing amide derivative |
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| Publication Number | Publication Date |
|---|---|
| JPH11302238A JPH11302238A (en) | 1999-11-02 |
| JP4143163B2 true JP4143163B2 (en) | 2008-09-03 |
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| Application Number | Title | Priority Date | Filing Date |
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| JP10921198A Expired - Fee Related JP4143163B2 (en) | 1998-04-20 | 1998-04-20 | Method for producing amide derivative |
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| JP (1) | JP4143163B2 (en) |
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| JPH11302238A (en) | 1999-11-02 |
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