JPH07258186A - Production of acylamino acid derivative - Google Patents

Production of acylamino acid derivative

Info

Publication number
JPH07258186A
JPH07258186A JP6050138A JP5013894A JPH07258186A JP H07258186 A JPH07258186 A JP H07258186A JP 6050138 A JP6050138 A JP 6050138A JP 5013894 A JP5013894 A JP 5013894A JP H07258186 A JPH07258186 A JP H07258186A
Authority
JP
Japan
Prior art keywords
acid derivative
formula
acrylic acid
acid amide
general formula
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.)
Pending
Application number
JP6050138A
Other languages
Japanese (ja)
Inventor
Toru Tsutsumi
徹 堤
Yohei Kaneko
洋平 金子
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.)
Kao Corp
Original Assignee
Kao Corp
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 Kao Corp filed Critical Kao Corp
Priority to JP6050138A priority Critical patent/JPH07258186A/en
Publication of JPH07258186A publication Critical patent/JPH07258186A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

PURPOSE:To readily produce an N-long chain acyamino acid useful as a low- stimulating activator, etc., or the derivative as its raw material at a low cost by reacting a fatty acid amide with a (meth)acrylic acid derivative in the presence of a base catalyst in an aprotic solvent. CONSTITUTION:This method for production of an acylamino acid derivative of the formula III (R<4> is H, a 1 to 4C alkyl or a group of the formula IV) is carried out by reacting (A) a fatty acid amide of the formula I (R<1>CO is a 8 to 22C fatty acid residue; R<2> is H, a 1 to 4C alkyl) with (B) a (meth)acrylic acid derivative (e.g. acrylonitrile, acrylic acid or acrylic acid amide) of the formula II (X is CO2R<2>, CN or CONH2; R<3> is H or CH3) in the presence of (C) a base catalyst [e.g. an alkaline (earth) metal alcoholate (1 to 3C), a hydroxide, etc.] in (D) an aprotic solvent (e.g. a hydrocarbon solvent or a halogenated hydrocarbon solvent). In addition, the amount of the component (B) is 0.6 to 2.0 times mole, preferably 0.8 to 1.5 time mole based on the component (A).

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、N−長鎖アシルアミノ
酸又はその原料として用いることのできるアシルアミノ
酸誘導体の製造法に関し、詳しくは、反応器の材質にと
らわれることなく、簡便な方法でかつ安価な原料を用い
て純度の高いアシルアミノ酸誘導体を製造する方法に関
するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing an N-long chain acylamino acid or an acylamino acid derivative which can be used as a raw material thereof, and more specifically, it is a simple method which is not restricted by the material of the reactor and The present invention relates to a method for producing a highly pure acylamino acid derivative using an inexpensive raw material.

【0002】[0002]

【従来の技術及び発明が解決しようとする課題】N−長
鎖アシルアミノ酸及びその塩は優れた界面活性作用や静
菌作用などを有し、低刺激性であることから様々な分野
において用いられている。従来、N−長鎖アシルアミノ
酸塩の製造法としては、アルカリ物質存在下アミノ酸と
脂肪酸ハライドを反応させるショッテン−バウマン(Sc
hotten−Baumann)反応が知られている(特公昭46−8685
号、特公昭51−38681 号、特開平4−368378号、特開平
5−7041号各公報)。しかし、ショッテン−バウマン反
応又はその改良法を用いた場合、いずれにしても原料と
してアミノ酸及び脂肪酸ハライドを用いる必要があり、
それらはいずれも工業的に入手するには高価であり、ま
た、脂肪酸ハライドを取り扱う材質に制限がある等の欠
点がある。
2. Description of the Related Art N-long-chain acylamino acids and salts thereof have excellent surfactant activity, bacteriostatic activity, etc. and are hypoallergenic, and are therefore used in various fields. ing. Conventionally, as a method for producing an N-long chain acylamino acid salt, Schotten-Baumann (Sc
hotten-Baumann) reaction is known (Japanese Patent Publication No. 46-8685).
JP-B-51-38681, JP-A-4-368378 and JP-A-5-7041). However, when the Schotten-Baumann reaction or an improved method thereof is used, it is necessary to use amino acids and fatty acid halides as raw materials in any case,
All of them have the drawbacks that they are expensive to obtain industrially, and that the materials for handling fatty acid halides are limited.

【0003】一方、このような欠点のあるアミノ酸及び
脂肪酸ハライドの代わりに安価な原料であるアシルアミ
ノ酸誘導体を用いることが提案されており、又、このア
シルアミノ酸誘導体が脂肪酸アミドとアクリル酸誘導体
から得られることも既に知られているが(USP 3138606
、USP 302133、FP 1392760、BP 875134 、BP 87
5135)、この方法では溶媒としてメタノール、ホル
ムアミド等のプロトン性溶媒を用いており、反応率が低
いという欠点がある。
On the other hand, it has been proposed to use an acylamino acid derivative which is an inexpensive raw material in place of the amino acid and fatty acid halide having such a defect, and the acylamino acid derivative is obtained from a fatty acid amide and an acrylic acid derivative. It is already known that it will be (USP 3138606
, USP 302133, FP 1392760, BP 875134, BP 87
5135), this method uses a protic solvent such as methanol or formamide as a solvent, and has a drawback that the reaction rate is low.

【0004】従って、本発明の目的は、N−長鎖アシル
アミノ酸又はその原料として有用なアシルアミノ酸誘導
体の工業生産に適した効率的な製造法を提供することに
ある。
Therefore, an object of the present invention is to provide an efficient production method suitable for industrial production of N-long chain acylamino acids or acylamino acid derivatives useful as raw materials thereof.

【0005】[0005]

【課題を解決するための手段】本発明者らは、鋭意検討
の結果、脂肪酸アミドとアクリル酸誘導体を塩基性触媒
存在下反応させるに際し、非プロトン性溶媒を用いるこ
とにより上記課題を解決出来ることを見い出し、本発明
を完成した。すなわち、本発明は、一般式(1)
Means for Solving the Problems As a result of intensive studies, the present inventors have found that the above problems can be solved by using an aprotic solvent when reacting a fatty acid amide with an acrylic acid derivative in the presence of a basic catalyst. The inventors have found out and completed the present invention. That is, the present invention, the general formula (1)

【0006】[0006]

【化5】 [Chemical 5]

【0007】(式中、R1CO- は炭素数8〜22の飽和又は
不飽和の脂肪酸残基を示し、R2はH 又は炭素数1〜4の
直鎖又は分岐のアルキル基を示す。)で表される脂肪酸
アミドと、一般式(2)
(In the formula, R 1 CO- represents a saturated or unsaturated fatty acid residue having 8 to 22 carbon atoms, and R 2 represents H or a linear or branched alkyl group having 1 to 4 carbon atoms. ) A fatty acid amide represented by the general formula (2)

【0008】[0008]

【化6】 [Chemical 6]

【0009】〔式中、X は−CO2R2(R2は前記の意味を示
す)、−CN又は−CONH2 を示し、R3はH 又は−CH3 を示
す。〕で表される(メタ)アクリル酸誘導体を、塩基性
触媒存在下、非プロトン性溶媒中で反応させることを特
徴とする、一般式(3)
[In the formula, X represents —CO 2 R 2 (R 2 has the above meaning), —CN or —CONH 2 , and R 3 represents H or —CH 3 . ] The (meth) acrylic acid derivative represented by the formula (3) is characterized by reacting in the presence of a basic catalyst in an aprotic solvent.

【0010】[0010]

【化7】 [Chemical 7]

【0011】〔式中、R,R3及びX は前記の意味を示
し、R4は H、炭素数1〜4の直鎖又は分岐のアルキル
基、又は式
[Wherein R 1 , R 3 and X have the above-mentioned meanings, R 4 is H, a linear or branched alkyl group having 1 to 4 carbon atoms, or

【0012】[0012]

【化8】 [Chemical 8]

【0013】(式中、R3及びX は前記の意味を示す)で
表される基を示す。〕で表されるアシルアミノ酸誘導体
の製造法を提供するものである。
(Wherein R 3 and X are as defined above). ] The manufacturing method of the acyl amino acid derivative represented by these is provided.

【0014】一般式(1) において、R1COは、直鎖又は分
岐の炭素数8〜22、好ましくは炭素数12〜18の飽和又は
不飽和の脂肪酸残基である。また、R2はH 又は炭素数1
〜4、好ましくは炭素数1〜3のアルキル基である。一
般式(1) で表される脂肪酸アミドとしては、具体的に
は、ラウリン酸アミド、パルミチン酸アミド、ステアリ
ン酸アミド、オレイン酸アミド、N−メチルラウリン酸
アミド、N−エチルラウリン酸アミドなどの単一組成の
脂肪酸アミドや、ヤシ油脂肪酸アミド、牛脂脂肪酸アミ
ドなどの混合脂肪酸のアミドが挙げられる。これらはい
ずれの方法で製造されたものでもよいが、例えば、脂肪
酸とアミンあるいはアンモニアをシリカゲル(油化学,
15,406(1966))やTi(O−i-C3H7)4(特開昭47−168 号)
等の触媒の存在下、反応させて得ることが出来る。
In the general formula (1), R 1 CO is a linear or branched saturated or unsaturated fatty acid residue having 8 to 22 carbon atoms, preferably 12 to 18 carbon atoms. R 2 is H or 1 carbon
To 4, preferably an alkyl group having 1 to 3 carbon atoms. Specific examples of the fatty acid amide represented by the general formula (1) include lauric acid amide, palmitic acid amide, stearic acid amide, oleic acid amide, N-methyllauric acid amide and N-ethyllauric acid amide. Examples include fatty acid amides having a single composition and amides of mixed fatty acids such as coconut oil fatty acid amide and tallow fatty acid amide. Although these may be produced by any method, for example, a fatty acid and an amine or ammonia are added to silica gel (oil chemistry,
15 , 406 (1966)) and Ti (O-iC 3 H 7 ) 4 (JP-A-47-168)
It can be obtained by reacting in the presence of a catalyst such as.

【0015】一般式(2)において、X は−CO2R2(R2は前
記の意味を示す)、−CN又は−CONHを示し、R
はH 又は−CH3 を示すが、好ましくはR3はH である。一
般式(2) で表される(メタ)アクリル酸誘導体の具体例
としては、アクリロニトリル、アクリル酸、アクリル酸
アミド、アクリル酸メチル、アクリル酸エチル等のアク
リル酸誘導体、メタクリロニトリル、メタクリル酸、メ
タクリル酸アミド、メタクリル酸メチル、メタクリル酸
エチル等のメタクリル酸誘導体が挙げられるが、好まし
くはアクリル酸誘導体で、特にアクリロニトリル、アク
リル酸メチル、アクリル酸エチルであり、アクリロニト
リルがより好ましい。これらは市販品を利用することが
出来る。
In the general formula (2), X represents --CO 2 R 2 (R 2 has the above meaning), --CN or --CONH 2 , and R 3
Represents H or -CH 3 , but preferably R 3 is H. Specific examples of the (meth) acrylic acid derivative represented by the general formula (2) include acrylonitrile, acrylic acid, acrylic acid amide, methyl acrylate, acrylic acid derivatives such as ethyl acrylate, methacrylonitrile, methacrylic acid, Methacrylic acid amide, methyl methacrylate, ethyl methacrylate, and other methacrylic acid derivatives are mentioned, but acrylic acid derivatives are preferable, and acrylonitrile, methyl acrylate, and ethyl acrylate are particularly preferable, and acrylonitrile is more preferable. These can be commercially available products.

【0016】本発明に用いられる塩基性触媒としては、
塩基性を示すものならいずれでもよいが、取り扱いの容
易さ、価格などの点よりアルカリ金属又はアルカリ土類
金属のアルコラート(炭素数1〜3、好ましくは1〜
2)、水酸化物あるいは炭酸塩等が好ましく、ナトリウ
ムメチラート、ナトリウムエチラート、カリウムメチラ
ート、水酸化ナトリウム、水酸化カリウムが特に好まし
い。塩基性触媒の使用量は一般式(2) で表される(メ
タ)アクリル酸誘導体に対し、5〜30モル%が好まし
く、より好ましくは10〜20モル%である。塩基性触媒の
使用量が5モル%よりも少ないと、反応時間が増大し工
業的に効率が悪くなり、30モル%より多いと反応時間の
短縮の効果もほとんどなく経済的に無駄である。
The basic catalyst used in the present invention includes
Any of those showing basicity may be used, but from the viewpoints of ease of handling, price, etc., an alkali metal or alkaline earth metal alcoholate (having 1 to 3 carbon atoms, preferably 1 to 3 carbon atoms).
2), hydroxides or carbonates are preferred, and sodium methylate, sodium ethylate, potassium methylate, sodium hydroxide, potassium hydroxide are particularly preferred. The amount of the basic catalyst used is preferably 5 to 30 mol% and more preferably 10 to 20 mol% based on the (meth) acrylic acid derivative represented by the general formula (2). When the amount of the basic catalyst used is less than 5 mol%, the reaction time increases and the efficiency is industrially deteriorated. When the amount used exceeds 30 mol%, the reaction time is hardly shortened and it is economically wasteful.

【0017】本発明に用いられる非プロトン性溶媒と
は、水、アルコール類、カルボン酸などのような分子間
に水素結合を作る溶媒ではなく、分子間に水素結合を作
ることの出来ない溶媒を言い、好ましくは炭化水素系溶
媒、ハロゲン化炭化水素系溶媒が挙げられ、脂肪族炭化
水素、芳香族炭化水素及びそれらのハロゲン化物等が挙
げられる。好ましい具体的非プロトン性溶媒としては、
ベンゼン、トルエン、キシレン、クロロベンゼン、o−
ジクロロベンゼン、m−ジクロロベンゼン、p−ジクロ
ロベンゼン、ヘキサン、シクロヘキサンなどが挙げられ
る。
The aprotic solvent used in the present invention is not a solvent such as water, alcohols and carboxylic acids which forms a hydrogen bond between molecules, but a solvent which cannot form a hydrogen bond between molecules. That is, hydrocarbon-based solvents and halogenated hydrocarbon-based solvents are preferred, and aliphatic hydrocarbons, aromatic hydrocarbons and their halides are preferred. As a preferred specific aprotic solvent,
Benzene, toluene, xylene, chlorobenzene, o-
Examples thereof include dichlorobenzene, m-dichlorobenzene, p-dichlorobenzene, hexane and cyclohexane.

【0018】本発明の方法によれば、一般式(1) で表さ
れる脂肪酸アミドと、好ましくはその 0.6〜2.0 モル
倍、より好ましくは 0.8〜1.5 モル倍の一般式(2) で表
される(メタ)アクリル酸誘導体を、塩基性触媒存在
下、一般式(1) で表される脂肪酸アミドに対し、 0.1〜
20重量倍、好ましくは 0.5〜10重量倍の非プロトン性溶
媒中、60〜140 ℃、好ましくは80〜120 ℃で反応させる
ことにより一般式(3) で表されるアシルアミノ酸誘導体
を得ることが出来る。なお、反応温度が140 ℃より高温
になるとアシルアミノ酸誘導体の分解が起こり、好まし
くない。又、塩基性触媒を水溶液あるいはアルコール溶
液として反応系に添加する時は、添加後、一般式(1) で
表される脂肪酸アミドと一般式(2) で表される(メタ)
アクリル酸誘導体を反応させる前に、水あるいはアルコ
ール等のプロトン性溶媒が本願発明の効果を害さない程
度の量になるまで減圧下留去する等の方法で除去するこ
とが好ましい。
According to the method of the present invention, the fatty acid amide represented by the general formula (1) is represented by the general formula (2), preferably 0.6 to 2.0 mol times, more preferably 0.8 to 1.5 mol times thereof. (Meth) acrylic acid derivative in the presence of a basic catalyst to the fatty acid amide represented by the general formula (1) in an amount of 0.1 to
It is possible to obtain an acylamino acid derivative represented by the general formula (3) by reacting in an aprotic solvent of 20 times by weight, preferably 0.5 to 10 times by weight, at 60 to 140 ° C, preferably 80 to 120 ° C. I can. When the reaction temperature is higher than 140 ° C, the acylamino acid derivative is decomposed, which is not preferable. When the basic catalyst is added to the reaction system as an aqueous solution or alcohol solution, after addition, the fatty acid amide represented by the general formula (1) and the general formula (2) (meta) are added.
Before the reaction of the acrylic acid derivative, it is preferable to remove the protic solvent such as water or alcohol by distilling under reduced pressure until the amount of the protic solvent does not impair the effects of the present invention.

【0019】また、一般式(1) で表される脂肪酸アミド
において、R2がH のとき、この脂肪酸アミドと一般式
(2) で表される(メタ)アクリル酸誘導体とのモル比
((メタ)アクリル酸誘導体/脂肪酸アミド)を 1.0以
上、特に2以上にすると、一般式(4) で表される2つの
置換基を持つ3級アミドが得られる。この2つの置換基
を持つ3級アミドもN−長鎖アシルアミノ酸の製造原料
として用いることができる。
In the fatty acid amide represented by the general formula (1), when R 2 is H, the fatty acid amide and the general formula
When the molar ratio with the (meth) acrylic acid derivative represented by (2) ((meth) acrylic acid derivative / fatty acid amide) is 1.0 or more, particularly 2 or more, two substitutions represented by the general formula (4) are performed. A tertiary amide bearing a group is obtained. A tertiary amide having these two substituents can also be used as a raw material for producing an N-long chain acylamino acid.

【0020】[0020]

【化9】 [Chemical 9]

【0021】(式中、R1, R3及びX は前記と同じ意味を
示す。) このようにして得られた一般式(3) で表されるアシルア
ミノ酸誘導体はそのまま各種反応原料などとして利用で
きるが、要すれば蒸留、再結晶などの精製工程を行えば
よい。一般に再結晶には濾過器、乾燥器といった工業上
付加がかかる設備が必要であり、また溶剤を使用するた
め、その回収設備も必要となり蒸留精製が好ましい。
(In the formula, R 1 , R 3 and X have the same meanings as described above.) The acylamino acid derivative represented by the general formula (3) thus obtained is used as it is as a raw material for various reactions. However, if necessary, a purification step such as distillation or recrystallization may be performed. Generally, recrystallization requires facilities such as a filter and a dryer to be added industrially, and since a solvent is used, a recovery facility for the solvent is also required, and distillation purification is preferable.

【0022】このようにして得られた一般式(3) で表さ
れるアシルアミノ酸誘導体は公知の方法により加水分解
され界面活性剤として有用な下記式(5) で表されるN−
長鎖アシルアミノ酸又はその塩に導くことが出来る。
The acylamino acid derivative represented by the general formula (3) thus obtained is hydrolyzed by a known method and is useful as a surfactant in the N-type represented by the following formula (5).
It can lead to long-chain acyl amino acids or salts thereof.

【0023】[0023]

【化10】 [Chemical 10]

【0024】(式中、R1,R2及びR3は前記の意味を示
し、M はH 又は陽イオンを示す。) 即ち、例えば一般式(3) において、X が−CNであるアミ
ドニトリルの場合、塩基性物質の存在下、加水分解する
ことにより、容易にN−長鎖アシルアミノ酸塩を得るこ
とができ、更に必要により鉱酸でpH1〜5に調整するこ
とによりN−長鎖アシルアミノ酸を得ることができる。
(In the formula, R 1 , R 2 and R 3 have the above-mentioned meanings, M represents H or a cation.) That is, for example, in the general formula (3), amidonitrile in which X is —CN. In the case of, the N-long-chain acylamino acid salt can be easily obtained by hydrolysis in the presence of a basic substance, and if necessary, the pH of the N-long-chain acylamino acid can be adjusted by adjusting the pH to 1 to 5 with a mineral acid. Amino acids can be obtained.

【0025】[0025]

【発明の効果】本発明の製造方法によれば、低刺激性活
性剤などとしてきわめて有用なN−長鎖アシルアミノ酸
又はその原料として有用なアシルアミノ酸誘導体を、反
応器の材質にとらわれることなく簡便な方法で、安価な
原料を用い、品質よく工業的に有利に製造することがで
きる。
EFFECTS OF THE INVENTION According to the production method of the present invention, an N-long chain acylamino acid which is extremely useful as a mild activator or the like, or an acylamino acid derivative which is useful as a raw material thereof, can be simply used without being restricted by the material of the reactor. Can be produced with good quality and industrially using various raw materials.

【0026】[0026]

【実施例】以下、実施例により本発明を詳細に説明する
が、本発明はこれら実施例に限定されるものではない。
なお、例中の%は特記しない限り重量基準である。収率
は特記されていないものは液体クロマトグラフィーによ
り定量し、ラウリン酸アミドに対するモル収率で示し
た。
The present invention will be described in detail below with reference to examples, but the present invention is not limited to these examples.
In the examples,% is based on weight unless otherwise specified. Unless otherwise specified, the yield was quantified by liquid chromatography and shown as a molar yield with respect to lauric acid amide.

【0027】実施例1 ラウリン酸アミド163.0 g(純度97.5%:0.80mol)、o
−ジクロロベンゼン1600g、28%ナトリウムメチラート
・メタノール溶液23.0g(15mol%対ラウリン酸アミド)
を攪拌機、ディーンスターク分留管、冷却管、温度計、
窒素導入管をつけた5リットルの5ツ口フラスコに入
れ、100℃まで加熱し均一溶液にした。100℃に加熱した
まま、窒素を吹き込み系内のメタノールを系外へ追い出
した。そこから温度を 120℃まで加熱し、重合禁止剤と
してヒドロキノンを少量添加し、アクリロニトリル63.3
g(1.5 当量 対ラウリン酸アミド) を1時間で滴下し
て反応させたところ、収率93.6%でN−ラウロイル−β
−アミノプロピオニトリルが得られた。
Example 1 163.0 g of lauric acid amide (purity 97.5%: 0.80 mol), o
-Dichlorobenzene 1600g, 28% sodium methylate / methanol solution 23.0g (15mol% to lauric acid amide)
A stirrer, Dean Stark fractionating tube, cooling tube, thermometer,
The mixture was placed in a 5-liter 5-necked flask equipped with a nitrogen introducing tube and heated to 100 ° C. to form a uniform solution. While heating at 100 ° C., nitrogen was blown in to expel the methanol in the system out of the system. From there, heat the temperature to 120 ° C, add a small amount of hydroquinone as a polymerization inhibitor, and add acrylonitrile 63.3
g (1.5 equivalents to lauric acid amide) was added dropwise over 1 hour to react with N-lauroyl-β with a yield of 93.6%.
-Aminopropionitrile was obtained.

【0028】実施例2 ラウリン酸アミド120.0g(純度97.5%:0.59mol)、o
−ジクロロベンゼン500g、21%ナトリウムエチラート
・エタノール溶液28.5g(15mol%対ラウリン酸アミド)
を攪拌機、ディーンスターク分留管、冷却管、温度計を
つけた1リットルの4ツ口フラスコに入れ、 120℃まで
加熱し均一溶液にし、重合禁止剤としてヒドロキノンを
少量添加し、アクリル酸エチル88.1g(1.5 当量 対ラ
ウリン酸アミド) を1時間で滴下して反応させたとこ
ろ、収率89.9%でN−ラウロイル−β−アミノプロピオ
ン酸エチルが得られた。
Example 2 120.0 g of lauric acid amide (purity 97.5%: 0.59 mol), o
-Dichlorobenzene 500g, 21% sodium ethylate / ethanol solution 28.5g (15mol% to lauric acid amide)
Was placed in a 1-liter 4-necked flask equipped with a stirrer, a Dean-Stark fractionating tube, a cooling tube, and a thermometer, heated to 120 ° C to make a uniform solution, and a small amount of hydroquinone as a polymerization inhibitor was added, and ethyl acrylate 88.1 When g (1.5 equivalents to lauric acid amide) was added dropwise for 1 hour to react, ethyl N-lauroyl-β-aminopropionate was obtained with a yield of 89.9%.

【0029】実施例3 ラウリン酸アミド20.5g(純度97.5%:0.10mol)、トル
エン101.5 g、30%カリウムメチラート・メタノール溶
液 3.5g(15mol%対ラウリン酸アミド)を攪拌機、ディ
ーンスターク分留管、冷却管、温度計をつけた300 ミリ
リットルの4ツ口フラスコに入れ、90℃まで加熱し均一
溶液にし、アクリル酸メチル12.9g(1.5当量 対ラウリ
ン酸アミド)を0.5 時間で滴下して反応させたところ、
収率90.1%でN−ラウロイル−β−アミノプロピオン酸
メチルが得られた。
Example 3 20.5 g of lauric acid amide (purity 97.5%: 0.10 mol), 101.5 g of toluene, 3.5 g of 30% potassium methylate-methanol solution (15 mol% relative to lauric acid amide) were stirred and a Dean-Stark fractionating tube. Put it in a 300 ml four-necked flask equipped with a cooling tube and a thermometer, heat it to 90 ° C to make a uniform solution, and add 12.9 g of methyl acrylate (1.5 equivalents to lauric acid amide) dropwise for 0.5 hours to react. Where
Methyl N-lauroyl-β-aminopropionate was obtained with a yield of 90.1%.

【0030】実施例4 ラウリン酸アミド163.0 g(純度97.5%:0.80mol)、o
−ジクロロベンゼン90g、20%水酸化カリウム・メタノ
ール溶液67.3g(30mol% 対ラウリン酸アミド) を攪拌
機、ディーンスターク分留管、冷却管、温度計、窒素導
入管をつけた5リットルの5ツ口フラスコに入れ、100
℃まで加熱し均一溶液にした。 100℃に加熱したまま、
窒素を吹き込み系内のメタノールを系外へ追い出した。
そこから温度を 120℃まで加熱し、重合禁止剤としてヒ
ドロキノンを少量添加し、アクリロニトリル169.2 g
(4.0 当量 対ラウリン酸アミド)を1時間で滴下して
反応させたところ、収率89.9%でN−ラウロイル−ビス
(β−アミノプロピオニトリル)が得られた。収率はガ
スクロマトグラフィーにより定量した。
Example 4 163.0 g of lauric acid amide (purity 97.5%: 0.80 mol), o
-Dichlorobenzene 90 g, 20% potassium hydroxide / methanol solution 67.3 g (30 mol% to lauric acid amide), a stirrer, a Dean-Stark fractionating pipe, a cooling pipe, a thermometer, a 5 liter 5 port equipped with a nitrogen inlet pipe. Put in a flask, 100
The mixture was heated to 0 ° C to form a uniform solution. While heating to 100 ℃,
Nitrogen was blown in to expel methanol in the system out of the system.
From there, heat the temperature to 120 ° C, add a small amount of hydroquinone as a polymerization inhibitor, and add 169.2 g of acrylonitrile.
When (4.0 equivalents to lauric acid amide) was added dropwise for 1 hour to react, N-lauroyl-bis (β-aminopropionitrile) was obtained with a yield of 89.9%. The yield was quantified by gas chromatography.

【0031】比較例1 ラウリン酸アミド10.0g(純度97.5%:0.049mol) 、ジ
メチルアセトアミド100.3 g、28%ナトリウムメチラー
ト・メタノール溶液1.4 g(15mol %、対ラウリン酸ア
ミド)を攪拌機、ディーンスターク分留管、冷却管、温
度計、窒素導入管をつけた200 ミリリットルの5ツ口フ
ラスコに入れ、100 ℃まで加熱し均一溶液にした。100
℃に加熱したまま、窒素を吹き込み系内のメタノールを
系外へ追い出した。そこから温度を 120℃まで加熱し、
重合禁止剤としてヒドロキノンを少量添加し、アクリロ
ニトリル3.9 g(1.5 当量 対ラウリン酸アミド)を
0.5時間で滴下して反応させたところ、収率36.2%でN
−ラウロイル−β−アミノプロピオニトリルが得られ
た。
Comparative Example 1 Lauric acid amide 10.0 g (purity 97.5%: 0.049 mol), dimethylacetamide 100.3 g, 28% sodium methylate / methanol solution 1.4 g (15 mol%, relative to lauric acid amide) were added with a stirrer and Dean Stark. The mixture was placed in a 200 ml 5-necked flask equipped with a distillation tube, a cooling tube, a thermometer, and a nitrogen introduction tube, and heated to 100 ° C. to form a uniform solution. 100
With heating at ℃, nitrogen was blown in to expel the methanol in the system out of the system. From there, heat up to 120 ° C,
Add a small amount of hydroquinone as a polymerization inhibitor and add 3.9 g of acrylonitrile (1.5 equivalents to lauric acid amide).
When dropped and reacted for 0.5 hours, the yield was 36.2% and N
-Lauroyl-β-aminopropionitrile was obtained.

【0032】比較例2 比較例1においてジメチルアセトアミド100.3 gをメタ
ノール100.3 gに変えた以外は同様の反応を行ったとこ
ろ、N−ラウロイル−β−アミノプロピオニトリルは検
出されなかった。
Comparative Example 2 N-lauroyl-β-aminopropionitrile was not detected in the same reaction as Comparative Example 1 except that 100.3 g of dimethylacetamide was changed to 100.3 g of methanol.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C07C 255/29 // C07B 61/00 300 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display location C07C 255/29 // C07B 61/00 300

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 一般式(1) 【化1】 (式中、R1CO- は炭素数8〜22の飽和又は不飽和の脂肪
酸残基を示し、R2はH 又は炭素数1〜4の直鎖又は分岐
のアルキル基を示す。)で表される脂肪酸アミドと、一
般式(2) 【化2】 〔式中、X は−CO2R2(R2は前記の意味を示す)、−CN又
は−CONH2 を示し、R3はH 又は−CH3 を示す。〕で表さ
れる(メタ)アクリル酸誘導体を、塩基性触媒存在下、
非プロトン性溶媒中で反応させることを特徴とする、一
般式(3) 【化3】 〔式中、R1,R3及びX は前記の意味を示し、R4は H、炭
素数1〜4の直鎖又は分岐のアルキル基、又は式 【化4】 (式中、R3及びX は前記の意味を示す)で表される基を
示す。〕で表されるアシルアミノ酸誘導体の製造法。
1. A general formula (1): (In the formula, R 1 CO- represents a saturated or unsaturated fatty acid residue having 8 to 22 carbon atoms, and R 2 represents H or a linear or branched alkyl group having 1 to 4 carbon atoms.) And a general formula (2): [In the formula, X represents —CO 2 R 2 (R 2 has the above-mentioned meaning), —CN or —CONH 2 , and R 3 represents H or —CH 3 . ] (Meth) acrylic acid derivative represented by, in the presence of a basic catalyst,
General formula (3): characterized by reacting in an aprotic solvent [Wherein R 1 , R 3 and X have the above-mentioned meanings, R 4 is H, a linear or branched alkyl group having 1 to 4 carbon atoms, or a compound represented by the formula: (In the formula, R 3 and X have the above-mentioned meanings). ] The manufacturing method of the acyl amino acid derivative represented by these.
【請求項2】 一般式(2) で表される(メタ)アクリル
酸誘導体が、アクリロニトリル、アクリル酸、アクリル
酸アミド、アクリル酸メチル又はアクリル酸エチルであ
る請求項1記載のアシルアミノ酸誘導体の製造法。
2. The production of an acylamino acid derivative according to claim 1, wherein the (meth) acrylic acid derivative represented by the general formula (2) is acrylonitrile, acrylic acid, acrylic acid amide, methyl acrylate or ethyl acrylate. Law.
【請求項3】 塩基性触媒がアルカリ金属又はアルカリ
土類金属のアルコラート(炭素数1〜3)、水酸化物あ
るいは炭酸塩である請求項1記載のアシルアミノ酸誘導
体の製造法。
3. The method for producing an acylamino acid derivative according to claim 1, wherein the basic catalyst is an alkali metal or alkaline earth metal alcoholate (having 1 to 3 carbon atoms), a hydroxide or a carbonate.
【請求項4】 非プロトン性溶媒が炭化水素系溶媒又は
ハロゲン化炭化水素系溶媒である請求項1記載のアシル
アミノ酸誘導体の製造法。
4. The method for producing an acylamino acid derivative according to claim 1, wherein the aprotic solvent is a hydrocarbon solvent or a halogenated hydrocarbon solvent.
JP6050138A 1994-03-22 1994-03-22 Production of acylamino acid derivative Pending JPH07258186A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6050138A JPH07258186A (en) 1994-03-22 1994-03-22 Production of acylamino acid derivative

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6050138A JPH07258186A (en) 1994-03-22 1994-03-22 Production of acylamino acid derivative

Publications (1)

Publication Number Publication Date
JPH07258186A true JPH07258186A (en) 1995-10-09

Family

ID=12850794

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6050138A Pending JPH07258186A (en) 1994-03-22 1994-03-22 Production of acylamino acid derivative

Country Status (1)

Country Link
JP (1) JPH07258186A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100511429B1 (en) * 1997-11-25 2005-11-08 주식회사 엘지생활건강 Process for preparing N-acyl-N-alkyl amido polyol carboxyalkyl ether type anionic surfactant

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100511429B1 (en) * 1997-11-25 2005-11-08 주식회사 엘지생활건강 Process for preparing N-acyl-N-alkyl amido polyol carboxyalkyl ether type anionic surfactant

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