JP2999305B2 - Method for producing imidazoline compound with low diamide content - Google Patents

Method for producing imidazoline compound with low diamide content

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Publication number
JP2999305B2
JP2999305B2 JP3222706A JP22270691A JP2999305B2 JP 2999305 B2 JP2999305 B2 JP 2999305B2 JP 3222706 A JP3222706 A JP 3222706A JP 22270691 A JP22270691 A JP 22270691A JP 2999305 B2 JP2999305 B2 JP 2999305B2
Authority
JP
Japan
Prior art keywords
reaction
acid
imidazoline
imidazoline compound
producing
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 - Fee Related
Application number
JP3222706A
Other languages
Japanese (ja)
Other versions
JPH0559013A (en
Inventor
孝四郎 外谷
浩之 井元
誠 久保
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
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Filing date
Publication date
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Priority to JP3222706A priority Critical patent/JP2999305B2/en
Publication of JPH0559013A publication Critical patent/JPH0559013A/en
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Publication of JP2999305B2 publication Critical patent/JP2999305B2/en
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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

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  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

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、ジアミンと脂肪酸又は
そのエステルとを反応させ、イミダゾリンを製造する
際、リン酸を添加することにより副生成物であるジアミ
ド含量の少ない高品質のイミダゾリン化合物を製造する
方法に関するものである。
BACKGROUND OF THE INVENTION The present invention relates to a method for producing imidazoline by reacting a diamine with a fatty acid or an ester thereof to obtain a high-quality imidazoline compound having a small amount of diamide as a by-product by adding phosphoric acid. It relates to a manufacturing method.

【0002】[0002]

【従来の技術及びその課題】イミダゾリン環構造を有
し、一位をアルキロール基により置換された化合物(以
後イミダゾリン化合物と記す)はイミダゾリン型界面活
性剤の有用な中間体として知られている。事実、市販さ
れているシャンプーの一部にはこの界面活性剤が使用さ
れている。特に近年、洗浄剤等に用いられる界面活性剤
は、界面活性能の他に生分解性、安全性、皮膚に対して
低刺激である等諸特性に優れたものが要望されており、
これらの要件を満たす界面活性剤の一つにイミダゾリン
型界面活性剤がある。イミダゾリン型界面活性剤は優れ
た起泡力、洗浄力に加え、眼や皮膚に対する刺激が極め
て低いという特徴があり、近年低刺激性シャンプー等の
主要成分としてその使用量が増加している。
2. Description of the Related Art Compounds having an imidazoline ring structure and substituted at one position by an alkylol group (hereinafter referred to as imidazoline compounds) are known as useful intermediates of imidazoline surfactants. In fact, some of the shampoos on the market use this surfactant. Particularly in recent years, surfactants used in detergents and the like are required to be excellent in various properties such as biodegradability, safety, and low irritation to the skin, in addition to the surfactant activity,
One of the surfactants satisfying these requirements is an imidazoline-type surfactant. The imidazoline-type surfactant is characterized by extremely low irritation to the eyes and skin in addition to excellent foaming and detergency, and its use as a major component of hypoallergenic shampoos and the like has recently been increasing.

【0003】このように、イミダゾリン化合物は種々の
イミダゾリン型界面活性剤の中間体として有用であるの
みならず、それ自体も界面活性剤として多用されてい
る。この場合イミダゾリン化合物の品質に要求される点
としては、副生成物であるジアミドの含量が低いこと、
色相の良好なこと等が挙げられる。
[0003] As described above, imidazoline compounds are not only useful as intermediates of various imidazoline-type surfactants, but also themselves are frequently used as surfactants. In this case, the point required for the quality of the imidazoline compound is that the content of the by-product diamide is low,
Good hue and the like.

【0004】イミダゾリン化合物は高級脂肪酸とジアミ
ンとを脱水縮合させることにより製造される。一般的に
この縮合反応は、適当な量の脂肪酸またはそのエステル
を使用すると、まずそのアミドアミンが生成し(反応式
)、次にこれが環化して所定のイミダゾリン環が生成
する(反応式)。この反応は脂肪酸を原料として用い
た場合、次のように例示することができる。
[0004] Imidazoline compounds are produced by dehydrating and condensing higher fatty acids and diamines. Generally, in the condensation reaction, when an appropriate amount of a fatty acid or an ester thereof is used, the amidoamine is first formed (reaction formula), and then this is cyclized to form a predetermined imidazoline ring (reaction formula). When a fatty acid is used as a raw material, this reaction can be exemplified as follows.

【0005】[0005]

【化2】 Embedded image

【0006】かかるジアミドは、水に対する溶解性に乏
しく、ジアミド含量の多いイミダゾリン化合物をシャン
プー等の最終製品に原料として用いた場合には、製品系
での濁りの原因となるばかりでなく、各種添加剤の溶解
性を阻害し、商品の外観あるいは商品が本来有する性能
をも著しく損ねるケースが多々ある。
[0006] Such a diamide has poor solubility in water, and when an imidazoline compound having a large diamide content is used as a raw material in a final product such as a shampoo, not only causes turbidity in the product system but also various additions. In many cases, the solubility of the agent is impaired, and the appearance of the product or the performance inherent in the product is significantly impaired.

【0007】低ジアミド含量のイミダゾリン化合物の製
造方法としては、例えば特公昭61−39939 号ではジアミ
ンの蒸気圧より高い特定の圧力下で反応させる方法が、
また特開昭54−63078 号では圧力を時間に対して対数的
に低下させる方法等が開示されている。前者の方法は、
1モルのヤシ油脂肪酸と1.05モル倍のジアミンとを所定
の反応容器に仕込んだ後に180 ℃まで昇温し、その後18
0 ℃近傍に反応温度を保持しながら反応圧力を100mmHg
まで低下させた後に、この圧力と180 ℃近傍の温度を5
時間維持し、所望の製品を得ようとするものである。即
ち、この方法はジアミンの蒸気圧より高い特定の圧力下
で反応を行い、ジアミド含量の少ないイミダゾリン化合
物を得ようとするものである。しかしながら、かかる方
法において、その実施例には 3.2〜4.0 %程度のジアミ
ドが製品中に含まれるように記載されているが、その方
法を実施した場合(本願比較例4)、実際には10%程度
のジアミドが製品中に含まれることが判明し、製品品質
として充分に満足されるものではなかった。また、後者
の方法は、反応時間が長く、色相等の他の品質が損なわ
れる可能性が高く、しかも反応圧力を時間に対して対数
的に低下させて反応を行う等、反応操作が煩雑であり、
合理的な製法とは言えない。
As a method for producing an imidazoline compound having a low diamide content, for example, Japanese Patent Publication No. 61-39939 discloses a method in which a reaction is carried out under a specific pressure higher than the vapor pressure of a diamine.
Japanese Patent Application Laid-Open No. 54-63078 discloses a method of decreasing the pressure logarithmically with respect to time. The former method is
1 mol of coconut oil fatty acid and 1.05 mol of diamine were charged into a predetermined reaction vessel, and then heated to 180 ° C.
While maintaining the reaction temperature near 0 ° C, increase the reaction pressure to 100 mmHg
After that, the pressure and the temperature around 180 ° C are reduced to 5
It is intended to maintain the time and obtain the desired product. That is, in this method, the reaction is carried out under a specific pressure higher than the vapor pressure of the diamine to obtain an imidazoline compound having a low diamide content. However, in such a method, although it is described in the examples that about 3.2 to 4.0% of diamide is contained in the product, when the method is performed (Comparative Example 4 of the present application), it is actually 10%. It was found that a certain amount of diamide was contained in the product, and the product quality was not satisfactory. In the latter method, the reaction time is long, there is a high possibility that other qualities such as hue are impaired, and the reaction operation is complicated, such as performing the reaction by decreasing the reaction pressure logarithmically with respect to time. Yes,
It is not a reasonable manufacturing method.

【0008】[0008]

【課題を解決するための手段】本発明者らは上記の従来
法の欠点を改善し、ジアミド含量が少ない高品質のイミ
ダゾリン化合物を簡単な操作で効率的に製造する方法を
開発するために鋭意研究を重ねた結果、高級脂肪酸また
はそのエステルとジアミンとを反応させる際、リン酸を
添加することにより低ジアミド含量のイミダゾリンが製
造できることを見出した。このような事実を示唆するい
かなる文献もなく、本発明者らはこの事実に到達するこ
とによって初めて、簡単な操作で効率的に高品質のイミ
ダゾリン化合物を製造することができるようになった。
DISCLOSURE OF THE INVENTION The present inventors have enthusiastically developed a method for improving the above-mentioned disadvantages of the conventional method and efficiently producing a high-quality imidazoline compound having a low diamide content by a simple operation. As a result of repeated studies, they have found that imidazoline having a low diamide content can be produced by adding phosphoric acid when reacting a higher fatty acid or its ester with a diamine. Without any literature suggesting such a fact, the present inventors were able to efficiently produce a high-quality imidazoline compound with a simple operation only by reaching this fact.

【0009】すなわち本発明は、一般式(1) R1COOR2 (1) (式中、R1は炭素数7〜21のアルキル基、アルケニル基
又はヒドロキシアルキル基を表し、R2はH又は低級アル
キル基を表す。)で表される高級脂肪酸又はそのエステ
ルと、一般式(2) H2NC2H4NHX (2) (式中、X は炭素数2〜4のアルキロール基を表す。)
で表されるジアミンとを反応させ、一般式(3)
[0009] The present invention has the general formula (1) R 1 COOR 2 ( 1) ( wherein, R 1 represents an alkyl group, an alkenyl group or hydroxyalkyl group having 7 to 21 carbon atoms, R 2 is H or A lower fatty acid group or a higher fatty acid thereof or an ester thereof, and a general formula (2) H 2 NC 2 H 4 NHX (2) (wherein X represents an alkylol group having 2 to 4 carbon atoms) .)
With a diamine represented by the general formula (3)

【0010】[0010]

【化3】 Embedded image

【0011】(式中、R1及びX は上記一般式(1) 、(2)
と同じ)で表されるイミダゾリン化合物を製造するにあ
たり、リン酸の存在下に反応を行なうことを特徴とする
低ジアミド含量イミダゾリン化合物の製造方法を提供す
るものである。本発明におけるリン酸とはオルトリン酸
のみならずピロリン酸、メタリン酸等の環状又は直鎖の
ポリリン酸をも含む概念である。
(Wherein, R 1 and X represent the above-mentioned general formulas (1) and (2)
The present invention provides a method for producing an imidazoline compound having a low diamide content, wherein the reaction is carried out in the presence of phosphoric acid in producing the imidazoline compound represented by the formula (1). The phosphoric acid in the present invention is a concept including not only orthophosphoric acid but also cyclic or linear polyphosphoric acid such as pyrophosphoric acid and metaphosphoric acid.

【0012】本発明に用いられる前記一般式(1) で表さ
れる高級脂肪酸又はそのエステルとしては、例えばカプ
リル酸、カプリン酸、ラウリン酸、ミリスチン酸、パル
ミチン酸、ステアリン酸、オレイン酸、ベヘニン酸、エ
ルカ酸、12−ヒドロキシステアリン酸、ヤシ油脂肪酸又
はこれらの高級脂肪酸のメチルエステル、エチルエステ
ル等を挙げることができる。
The higher fatty acid represented by the general formula (1) or an ester thereof used in the present invention includes, for example, caprylic acid, capric acid, lauric acid, myristic acid, palmitic acid, stearic acid, oleic acid, behenic acid , Erucic acid, 12-hydroxystearic acid, coconut oil fatty acids or methyl esters and ethyl esters of these higher fatty acids.

【0013】また、本発明に用いられる前記一般式(2)
で表されるジアミンとしては、例えば H2NC2H4NHC2H4O
H、H2NC2H4NHC3H6OH 等の化合物を挙げることができ
る。
The above-mentioned general formula (2) used in the present invention
As the diamine represented by, for example, H 2 NC 2 H 4 NHC 2 H 4 O
Compounds such as H and H 2 NC 2 H 4 NHC 3 H 6 OH can be mentioned.

【0014】本発明の製造方法において、高品質のイミ
ダゾリン化合物を得るための反応温度としては、 180〜
220 ℃が望ましい。反応温度が180 ℃以下ではイミダゾ
リン化(反応式における右方向への反応)の反応速度
が小さく且つ、ジアミドの分解速度(反応式における
左方向への反応)が小さい。その結果ジアミドが分解し
てイミダゾリン化合物へ変換する速度が小さいので、ジ
アミド含量を所望の水準まで低下させることが困難であ
る。また反応温度が 220℃以上では色調の劣化を招く結
果となる。
In the production method of the present invention, the reaction temperature for obtaining a high-quality imidazoline compound is 180-180.
220 ° C is preferred. When the reaction temperature is 180 ° C. or lower, the reaction rate of imidazoline formation (reaction to the right in the reaction formula) is low, and the decomposition rate of diamide (reaction to the left in the reaction formula) is low. As a result, the rate at which the diamide is decomposed and converted into the imidazoline compound is low, so that it is difficult to reduce the diamide content to a desired level. On the other hand, when the reaction temperature is higher than 220 ° C., the color tone is deteriorated.

【0015】本発明の製造方法における反応圧力は、生
成する水を効率的に排除できる程度であれば問題ない。
通常原料のジアミンが水と一緒に系外に出ない様に設定
することが必要である。アミド化では通常 400mmHg程度
であり、イミダゾリンへの閉環反応では 200mmHg以下が
好ましく、更に残存するジアミンの除去の工程では50mm
Hg以下、好ましくは10mmHg以下まで下げる方が良い。こ
のイミダゾリンの閉環時及びジアミン除去の工程でジア
ミドが分解し、モノアミド、更にはイミダゾリンへと変
換されるのである。
The reaction pressure in the production method of the present invention is not problematic as long as generated water can be efficiently removed.
Usually, it is necessary to set the starting material so that the diamine does not go out of the system together with water. In the case of amidation, it is usually about 400 mmHg, in the case of a ring closure reaction to imidazoline, it is preferably 200 mmHg or less, and in the step of removing remaining diamine, it is 50 mmHg.
Hg or less, preferably 10 mmHg or less. During the ring closure of the imidazoline and the step of removing the diamine, the diamide is decomposed and converted into a monoamide and further into an imidazoline.

【0016】本発明の方法において前記ジアミンと前記
高級脂肪酸又はそのエステルとのモル比は、通常1:1
ないし 1.5:1であり、1:1ないし 1.3:1が好まし
い。
In the method of the present invention, the molar ratio of the diamine to the higher fatty acid or its ester is usually 1: 1.
To 1.5: 1, preferably 1: 1 to 1.3: 1.

【0017】また、使用されるリン酸の量は、脂肪酸又
はそのエステルに対し0.01〜5モル%、好ましくは 0.1
〜3モル%である。リン酸の使用量がこの範囲より少な
い場合には所望の低ジアミド含量イミダゾリンが得難い
し、一方リン酸の使用量がこの範囲より多くてもこの範
囲以上の効果は期待できないので、経済的観点より好ま
しくない。
The amount of phosphoric acid used is from 0.01 to 5 mol%, preferably from 0.1 to 5 mol%, based on the fatty acid or its ester.
~ 3 mol%. If the amount of phosphoric acid used is less than this range, it is difficult to obtain the desired low diamide content imidazoline, while if the amount of phosphoric acid used is more than this range, effects beyond this range cannot be expected, so from an economic viewpoint. Not preferred.

【0018】リン酸の添加時期は最初から、即ち脂肪酸
又はそのエステルを仕込む時か、或いはアミド化が終了
しイミダゾリンへの閉環工程に移る段階でもよい。
The phosphoric acid may be added from the beginning, that is, when the fatty acid or its ester is charged, or when the amidation is completed and the process proceeds to the step of closing the ring to imidazoline.

【0019】本発明者らは、本発明のリン酸の添加によ
るイミダゾリンの製造で、驚くべきことに無添加系に比
べ著しく系内のジアミド含量が低下することを見出し
た。この理由の詳細は不明な部分が多いが、酸性である
リン酸がモノアミドのアミド部分に作用し、アミドの分
極を助けることによりイミダゾリン閉環反応を促進し、
即ち前記反応式の平衡をアミドアミン側よりイミダゾ
リン側にかたよらせ、同時に反応式において副生する
ジアミドの分解によるアミドアミンの再生を促進する。
つまり、ジアミドの分解によるアミドアミンの再生と再
生したアミドアミンのイミダゾリン化合物への変換を促
進させる作用によりジアミド含量が低くなるものと推定
される。
The present inventors have surprisingly found that the production of imidazoline by the addition of phosphoric acid of the present invention surprisingly lowers the diamide content in the system as compared with the non-added system. Although the details of this reason are largely unknown, the acidic phosphoric acid acts on the amide portion of the monoamide, promoting the imidazoline ring closure reaction by helping the amide polarization,
That is, the equilibrium of the above reaction formula is shifted from the amidoamine side to the imidazoline side, and at the same time, regeneration of amidoamine by decomposition of diamide by-produced in the reaction formula is promoted.
That is, it is presumed that the diamide content is reduced by the action of promoting the regeneration of the amidoamine by the decomposition of the diamide and the conversion of the regenerated amidoamine to the imidazoline compound.

【0020】このように本発明は高純度なイミダゾリン
の製造方法として有用である。
Thus, the present invention is useful as a method for producing high-purity imidazoline.

【0021】[0021]

【実施例】次に本発明を実施例により詳細に説明する
が、本発明はこれらによって限定されるものではない。
EXAMPLES Next, the present invention will be described in detail with reference to examples, but the present invention is not limited to these examples.

【0022】実施例1 攪拌機、温度計、還流冷却器、及び圧力計を備えた1リ
ットル容4ツ口フラスコに、ラウリン酸 200g (分子量
200 ,1モル)とアミノエチルエタノールアミン 109.2
g(分子量104 ,以下AEEAと略記)とを仕込んだ。還流
冷却器に80℃の温水を通しながら、上記混合物を攪拌し
140℃へ加熱した。その後反応圧力を1時間かけて 400
mmHgに設定し、2時間反応させアミド化を行なった。そ
の後、N2で常圧に戻し、オルトリン酸 0.98 g(分子量
98,0.01モル)を添加した。次に反応温度を 200℃、圧
力を1.5時間かけて 200mmHgまで下げ、この条件で1時
間熟成を行なった。更に圧力を約 1.5時間かけて10mmHg
まで下げ、この条件で1時間反応を行い過剰のAEEAを除
去した。この間、生成水及びAEEAの蒸気はドライアイス
/メタノール冷却トラップに捕集した。反応終了物は、
高速液体クロマトグラフィー(以下HPLCと略記)を用い
て組成分析を行なった。反応生成物の組成を表1に示
す。
Example 1 200 g of lauric acid (molecular weight) was placed in a 1-liter four-necked flask equipped with a stirrer, a thermometer, a reflux condenser, and a pressure gauge.
200, 1 mol) and aminoethylethanolamine 109.2
g (molecular weight: 104, hereinafter abbreviated as AEAA). The mixture was stirred while warm water at 80 ° C was passed through the reflux condenser.
Heated to 140 ° C. Thereafter, the reaction pressure was increased to 400 over 1 hour.
The reaction was set at mmHg and reacted for 2 hours to effect amidation. After that, the pressure was returned to normal pressure with N 2 , and orthophosphoric acid 0.98 g (molecular weight
98, 0.01 mol). Next, the reaction temperature was lowered to 200 mmHg over a period of 1.5 hours at a reaction temperature of 200 ° C., and aging was performed under these conditions for 1 hour. Further increase the pressure for about 1.5 hours to 10mmHg
The reaction was carried out for 1 hour under these conditions to remove excess AEAA. During this time, the generated water and the vapor of AEEA were collected in a dry ice / methanol cooling trap. The finished product is
Composition analysis was performed using high performance liquid chromatography (hereinafter abbreviated as HPLC). Table 1 shows the composition of the reaction product.

【0023】実施例2 ヤシ油脂肪酸メチルエステル 220.5g(分子量220.5 ,
1モル)とAEEA 109.2gを実施例1と同様な反応器に仕
込み、 160℃まで約1時間かけて昇温した。その後約1
時間かけて 200mmHgまで減圧し、その状態で1時間熟成
を行ないアミド化を行なった。次にN2で常圧に戻し、オ
ルトリン酸 2.94 g(0.03モル)を添加した。その後反
応温度を 200℃、圧力を 1.5時間かけて 200mmHgにし、
この条件で1時間熟成を行なった。更に圧力を約 1.5時
間かけて10mmHgまで下げ、この条件で1時間反応を行い
過剰のAEEAを除去した。この間、生成水、メタノール及
びAEEAの蒸気はドライアイス/メタノール冷却トラップ
に捕集した。反応終了物は、HPLCを用いて組成分析を行
なった。反応生成物の組成を表1に示す。
Example 2 220.5 g of coconut oil fatty acid methyl ester (molecular weight: 220.5,
1 mol) and 109.2 g of AEEA were charged into the same reactor as in Example 1, and the temperature was raised to 160 ° C. over about 1 hour. Then about 1
The pressure was reduced to 200 mmHg over time, and aging was performed for 1 hour in that state to perform amidation. Then, the pressure was returned to normal pressure with N 2 , and 2.94 g (0.03 mol) of orthophosphoric acid was added. After that, the reaction temperature was set to 200 ° C and the pressure was set to 200 mmHg over 1.5 hours.
Aging was performed under these conditions for one hour. The pressure was further reduced to 10 mmHg over about 1.5 hours, and the reaction was carried out for 1 hour under these conditions to remove excess AAEA. During this time, generated water, methanol, and vapors of AEEA were collected in a dry ice / methanol cooling trap. The finished product was subjected to composition analysis using HPLC. Table 1 shows the composition of the reaction product.

【0024】実施例3 オルトリン酸 0.1g(0.001 モル)をラウリン酸及びAE
EAと同時に仕込むこと及びこれ以外にはリン酸を添加し
ないことを除いては実施例1と同様に反応を行った。反
応生成物の組成を表1に示す。
Example 3 0.1 g (0.001 mol) of orthophosphoric acid was added to lauric acid and AE
The reaction was carried out in the same manner as in Example 1 except that EA was charged at the same time and no phosphoric acid was added. Table 1 shows the composition of the reaction product.

【0025】実施例4 オルトリン酸0.49g(0.005 モル)をヤシ油脂肪酸メチ
ルエステル及びAEEAと同時に仕込むこと及びこれ以外に
はリン酸を添加しないことを除いては実施例2と同様に
反応を行った。反応生成物の組成を表1に示す。
Example 4 A reaction was carried out in the same manner as in Example 2 except that 0.49 g (0.005 mol) of orthophosphoric acid was charged at the same time as the coconut oil fatty acid methyl ester and AEEA, and no phosphoric acid was added. Was. Table 1 shows the composition of the reaction product.

【0026】実施例5 オルトリン酸の代わりにピロリン酸 0.89 g(分子量17
8 ,0.005 モル)を使用することを除いては、実施例1
と同様に反応を行った。反応生成物の組成を表1に示
す。
Example 5 Instead of orthophosphoric acid, 0.89 g of pyrophosphoric acid (molecular weight: 17
8, 0.005 mol) of Example 1
The reaction was carried out in the same manner as described above. Table 1 shows the composition of the reaction product.

【0027】比較例1 実施例1でオルトリン酸を添加せずに反応を行なった。
反応生成物の組成を表1に示す。
Comparative Example 1 The reaction of Example 1 was carried out without adding orthophosphoric acid.
Table 1 shows the composition of the reaction product.

【0028】比較例2 実施例2でオルトリン酸を添加せずに反応を行なった。
反応生成物の組成を表1に示す。
Comparative Example 2 The reaction of Example 2 was carried out without adding orthophosphoric acid.
Table 1 shows the composition of the reaction product.

【0029】比較例3 実施例3でオルトリン酸の代わりに35%塩酸3.13g(0.
03モル)を加え、その後の条件は実施例3と同じで反応
を行なった。反応生成物の組成を表1に示す。
Comparative Example 3 In Example 3, 3.13 g (0.3%) of 35% hydrochloric acid was used instead of orthophosphoric acid.
03 mol), and the reaction was carried out under the same conditions as in Example 3. Table 1 shows the composition of the reaction product.

【0030】比較例4 実施例3でオルトリン酸の代わりに98%硫酸3g(0.03
モル)を加え、その後の条件は実施例3と同じで反応を
行なった。反応生成物の組成を表1に示す。
Comparative Example 4 In Example 3, 3 g of 98% sulfuric acid (0.03%) was used instead of orthophosphoric acid.
Mol), and the reaction was carried out under the same conditions as in Example 3. Table 1 shows the composition of the reaction product.

【0031】比較例5 実施例3でオルトリン酸の代わりにホウ酸(分子量61.
8)1.85g(0.03モル)を加え、その後の条件は実施例
3と同じで反応を行なった。反応生成物の組成を表1に
示す。
Comparative Example 5 In Example 3, boric acid (molecular weight: 61.20) was used instead of orthophosphoric acid.
8) 1.85 g (0.03 mol) was added, and the reaction was carried out under the same conditions as in Example 3. Table 1 shows the composition of the reaction product.

【0032】比較例6 低ジアミド含量のイミダゾリン製造法として特許公開さ
れている特公昭61−39939 号の方法に従ってイミダゾリ
ン化合物の合成を行なった。実施例1と同様の反応器を
使用し、攪拌しながら200 gのラウリン酸(分子量200
)とAEEA 109.2gとを仕込こみ、圧力を下げて 100mmH
gに達してから加熱を始めた。フラスコ内の温度が 130
℃に達し、反応生成水の流出が始まったら、昇温速度を
緩めて 180℃の反応温度まで到達させて3時間反応させ
た。その後反応圧力を10mmHgまで低下させ、過剰のAEEA
を除去した後に冷却した。反応終了物はHPLCを用いて組
成分析を行なった。反応生成物の組成を表1に示す。
Comparative Example 6 An imidazoline compound was synthesized according to the method of Japanese Patent Publication No. 61-39939, which was published as a method for producing imidazoline having a low diamide content. Using the same reactor as in Example 1, 200 g of lauric acid (molecular weight: 200
) And AEEA 109.2g, and reduce the pressure to 100mmH
After reaching g, heating was started. The temperature in the flask is 130
C., and when the flow of the reaction water began to flow, the temperature was raised slowly to reach a reaction temperature of 180.degree. C., and the reaction was carried out for 3 hours. Thereafter, the reaction pressure was reduced to 10 mmHg, and excess AEEA
After cooling, the mixture was cooled. The finished product was subjected to composition analysis using HPLC. Table 1 shows the composition of the reaction product.

【0033】[0033]

【表1】 [Table 1]

【0034】結 果 表1より明らかなように、実施例1〜5の場合には副生
成物であるジアミド成分含量が低く、かつイミダゾリン
化合物の含有量が高い。これに対して比較例1〜6のよ
うにリン酸を添加しない場合や、リン酸の代わりに塩
酸、硫酸、ホウ酸を添加した場合、或いは従来の反応条
件での低減方法では、ジアミド成分が多くしかもイミダ
ゾリン化合物の含有量も低いことが明らかである。
[0034] As is apparent from the results in Table 1, in the case of Examples 1 to 5 diamide ingredient content is low by-product, and high content of imidazoline compounds. On the other hand, when no phosphoric acid is added as in Comparative Examples 1 to 6, when hydrochloric acid, sulfuric acid, or boric acid is added instead of phosphoric acid, or in a conventional reduction method under reaction conditions, the diamide component is It is clear that the content is high and the content of the imidazoline compound is low.

【0035】[0035]

【発明の効果】本発明によれば、従来極めて困難と考え
られていた高品質のイミダゾリン化合物の製造が、ジア
ミンと、高級脂肪酸又はそのエステルとリン酸から簡単
に達成できる。しかも工業的な操作は極めて簡単であ
る。また、本発明の製造方法によって得られたイミダゾ
リン化合物は色相が良好で純度が高く、かつジアミドの
含量が低いために高品質のイミダゾリン化合物として各
種の用途に後処理を要せずにそのまま使用できる。
According to the present invention, the production of a high-quality imidazoline compound, which has conventionally been considered extremely difficult, can be easily achieved from a diamine, a higher fatty acid or its ester and phosphoric acid. Moreover, industrial operation is extremely simple. Further, the imidazoline compound obtained by the production method of the present invention can be used as a high-quality imidazoline compound without any post-treatment for various uses as a high-quality imidazoline compound because of its good hue, high purity, and low diamide content. .

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 一般式(1) R1COOR2 (1) (式中、R1は炭素数7〜21のアルキル基、アルケニル基
又はヒドロキシアルキル基を表し、R2はH又は低級アル
キル基を表す。)で表される高級脂肪酸又はそのエステ
ルと、一般式(2) H2NC2H4NHX (2) (式中、X は炭素数2〜4のアルキロール基を表す。)
で表されるジアミンとを反応させ、一般式(3) 【化1】 (式中、R1及びX は上記一般式(1) 、(2) と同じ)で表
されるイミダゾリン化合物を製造するにあたり、リン酸
の存在下に反応を行なうことを特徴とする低ジアミド含
量イミダゾリン化合物の製造方法。
A compound represented by the general formula (1): R 1 COOR 2 (1) wherein R 1 represents an alkyl group, an alkenyl group or a hydroxyalkyl group having 7 to 21 carbon atoms, and R 2 represents H or a lower alkyl group. And a higher fatty acid or an ester thereof represented by the general formula (2) H 2 NC 2 H 4 NHX (2) (wherein, X represents an alkylol group having 2 to 4 carbon atoms).
Is reacted with a diamine represented by the general formula (3). (Wherein, R 1 and X are the same as those of the above general formulas (1) and (2)). In producing an imidazoline compound, the reaction is carried out in the presence of phosphoric acid. A method for producing an imidazoline compound.
【請求項2】 リン酸の添加量が使用する高級脂肪酸又
はそのエステルに対し0.01〜5モル%である請求項1記
載の低ジアミド含量イミダゾリン化合物の製造方法。
2. The method for producing an imidazoline compound having a low diamide content according to claim 1, wherein the amount of phosphoric acid is 0.01 to 5 mol% based on the higher fatty acid or ester thereof used.
JP3222706A 1991-09-03 1991-09-03 Method for producing imidazoline compound with low diamide content Expired - Fee Related JP2999305B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3222706A JP2999305B2 (en) 1991-09-03 1991-09-03 Method for producing imidazoline compound with low diamide content

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3222706A JP2999305B2 (en) 1991-09-03 1991-09-03 Method for producing imidazoline compound with low diamide content

Publications (2)

Publication Number Publication Date
JPH0559013A JPH0559013A (en) 1993-03-09
JP2999305B2 true JP2999305B2 (en) 2000-01-17

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Family Applications (1)

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Country Link
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